US7651980B2 - High temperature filtration control using water based drilling fluid systems comprising water soluble polymers - Google Patents

High temperature filtration control using water based drilling fluid systems comprising water soluble polymers Download PDF

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US7651980B2
US7651980B2 US11/346,453 US34645306A US7651980B2 US 7651980 B2 US7651980 B2 US 7651980B2 US 34645306 A US34645306 A US 34645306A US 7651980 B2 US7651980 B2 US 7651980B2
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drilling fluid
fluid system
water soluble
soluble polymer
mole
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US20070179064A1 (en
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Michael Jarrett
Dennis Clapper
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Baker Hughes Holdings LLC
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Baker Hughes Inc
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Assigned to BAKER HUGHES INCORPORATED reassignment BAKER HUGHES INCORPORATED ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: CLAPPER, DENNIS, JARRETT, MICHAEL
Priority to AU2007212753A priority patent/AU2007212753B2/en
Priority to BRPI0707688-6A priority patent/BRPI0707688A2/en
Priority to PCT/US2007/001673 priority patent/WO2007092150A2/en
Priority to EP07763209A priority patent/EP1989273A4/en
Publication of US20070179064A1 publication Critical patent/US20070179064A1/en
Priority to NO20083368A priority patent/NO20083368L/en
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    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/02—Well-drilling compositions
    • C09K8/04—Aqueous well-drilling compositions
    • C09K8/06—Clay-free compositions
    • C09K8/12—Clay-free compositions containing synthetic organic macromolecular compounds or their precursors
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/50—Compositions for plastering borehole walls, i.e. compositions for temporary consolidation of borehole walls
    • C09K8/504—Compositions based on water or polar solvents
    • C09K8/506—Compositions based on water or polar solvents containing organic compounds
    • C09K8/508—Compositions based on water or polar solvents containing organic compounds macromolecular compounds
    • C09K8/5083—Compositions based on water or polar solvents containing organic compounds macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K2208/00—Aspects relating to compositions of drilling or well treatment fluids
    • C09K2208/18—Bridging agents, i.e. particles for temporarily filling the pores of a formation; Graded salts

Definitions

  • the present application relates to a method for providing filtration control during drilling operations at high temperatures.
  • the present application also relates to water based drilling fluid systems that achieve high temperature filtration control using water soluble polymers.
  • Filtration control is an important property of a drilling fluid, particularly when drilling through permeable formations where the hydrostatic pressure exceeds the formation pressure. It is important for a drilling fluid to quickly form a filter cake which effectively minimizes fluid loss, but which also is thin and erodable enough to allow product to flow into the wellbore during production.
  • water-soluble polymer typically comprising acrylamide monomer.
  • acrylamide monomer acrylamide monomer
  • Filtration control additives are needed which will quickly form a thin, erodable filter cake, and which have high temperature stability for prolonged periods of time.
  • the present application provides drilling fluid systems comprising water soluble polymer(s) comprising acrylamide monomer which exhibit effective rheological properties and high temperature high pressure (HTHP) filtration control at temperatures of 177° C. (350° F.) or more.
  • HTHP high temperature high pressure
  • the present application provides drilling fluid systems comprising water soluble polymer comprising acrylamide monomer which exhibit effective rheological properties and HTHP filtration control at temperatures of 260° C. (500° F.) or more.
  • the present application provides a method for providing filtration control during drilling operations using a drilling fluid system comprising water soluble polymer comprising acrylamide monomer, the method comprising: providing a drilling fluid system having effective rheological properties, the drilling fluid system comprising aqueous base consisting essentially of freshwater, a quantity of from about 21 to 58 kg/m 3 (7.5 to about 20 pounds per barrel) plugging agent, and an amount of bridging agent comprising water soluble polymer comprising acrylamide monomer which exhibits a 5% by weight Brookfield viscosity in freshwater of from about 50 cP to about 100 cP, and; contacting a subterranean formation with the drilling fluid system and maintaining effective filtration control at concentrations of about 10,000 ppm or less monovalent salt, as demonstrated in the laboratory by producing a HPHT filtrate of 25 cm 3 /min or less after 30 minutes at about 149° C. (300° F.) after static aging of said drilling fluid system for a period of 16 hours or more at temperatures of about
  • the present application also provides a drilling fluid system comprising: an aqueous base consisting essentially of freshwater; a quantity of from about 21 to 58 kg/m 3 (7.5 to 20 lb/bbl) plugging agent comprising sulfonated asphalt and lignite; bridging agent comprising an amount of water soluble polymer having a 5% by weight Brookfield viscosity in freshwater of from about 50 cP to about 100 cP, the water soluble polymer comprising first olefinic amide monomer copolymerized with monomer selected from the group consisting of sulfonate monomer and a combination of sulfonate monomer and N-vinyl lactam monomer, wherein the first olefinic amide monomer has the following structure:
  • the sulfonate monomer has the following structure:
  • N-vinyl lactam monomer has the following structure:
  • the drilling fluid system exhibits a HPHT filtrate of 25 cm 3 /min or less after 30 minutes at about 149° C. (300° F.).
  • the application provides a drilling fluid system comprising: an aqueous base consisting essentially of freshwater; bridging agent comprising from about 0.7 to about 29 kg/m 3 (0.25 lb/bbl to about 10.0 lb/bbl) water soluble polymer having a 5% by weight Brookfield viscosity in freshwater of from about 50 cP to about 100 cP, the water soluble polymer comprising acrylamide monomer copolymerized with monomer selected from the group consisting of sulfonate monomer and a combination of sulfonate monomer and N-vinyl lactam monomer; and, a quantity of from about 21 to 58 kg/m 3 (7.5 to 20 lb/bbl) plugging agent comprising sulfonated asphalt and lignite; wherein, after 16 hours of static aging of the drilling fluid system at about 260° C. (500° F.), the drilling fluid system exhibits a HPHT filtrate of 25 cm 3 /
  • the application provides a drilling fluid system comprising: an aqueous base consisting essentially of freshwater; bridging agent comprising from about 0.7 to about 29 kg/m 3 (0.25 lb/bbl to about 10.0 lb/bbl) water soluble polymer having a 5% by weight Brookfield viscosity in freshwater of from about 50 cP to about 100 cP, said water soluble polymer comprising monomer of acrylamide, monomer of 2-acrylamido-2-methylpropane sulfonic acid or alkali metal salts thereof, and N-vinyl pyrrolidone monomer; and, from about 21 to 58 kg/m 3 (7.5 to 20 lb/bbl) plugging agent comprising sulfonated asphalt and lignite; wherein, after 16 hours of static aging of the drilling fluid system at about 260° C. (500° F.), the drilling fluid system exhibits a HPHT filtrate of 25 cm 3 /min or less after 30 minutes
  • the application provides a drilling fluid system comprising: an aqueous base consisting essentially of freshwater; bridging agent comprising from about 0.7 to about 29 kg/m 3 (0.25 lb/bbl to about 10.0 lb/bbl) water soluble polymer having a 5% by weight Brookfield viscosity in freshwater of from about 50 to about 100 cP comprising monomers of acrylamide and 2-acrylamido-2-methylpropane sulfonic acid or alkali metal salts thereof; and, plugging agent comprising a quantity of from about 21 to 58 kg/m 3 (7.5 to 20 lb/bbl) sulfonated asphalt comprising lignite; wherein, after 16 hours of static aging of the drilling fluid system at about 260° C. (500° F.), the drilling fluid system exhibits a HPHT filtrate of 25 cm 3 /min or less after 30 minutes at about 149° C. (300° F.).
  • the present application provides a drilling fluid system which quickly forms a thin, erodable filter cake effective to minimize filtration of a drilling fluid system into the subterranean formation being treated.
  • the drilling fluid system is stable for a prolonged period of time even after exposure to high temperatures. Effective filtration control is demonstrated in the laboratory when, after 16 hours of static aging at the temperature of expected exposure, the drilling fluid system exhibits a HPHT filtrate of 25 cm 3 /min or less after 30 minutes at about 149° C. (300° F.). In one embodiment, the drilling fluid system exhibits a HPHT filtrate of 25 cm 3 /min or less after 30 minutes at about 177° C. (350° F.) or more.
  • the drilling fluid system maintains effective filtration control even after exposure to a temperature of 149° C. (300° F.) for a period of about 16 hours or more. In one embodiment, the drilling fluid system maintains effective filtration control even after exposure to a temperature of 177° C. (350° F.) for a period of about 16 hours or more. In one embodiment, the drilling fluid system maintains effective filtration control even after exposure to a temperature of 260° C. (500° F.) or more for a period of about 16 hours or more. In yet another embodiment, the drilling fluid system maintains effective filtration control even after exposure to a temperature of 287° C. (550° F.) or more for a period of about 16 hours or more.
  • the drilling fluid also is effective when exposed to 10,000 ppm or less monovalent salt. In one embodiment, the drilling fluid is exposed to 9,000 ppm or less monovalent salt.
  • the drilling fluid system comprises an aqueous base, water soluble polymer, and plugging agent.
  • the drilling fluid system also may contain other suitable components.
  • the aqueous base is freshwater.
  • the aqueous base may comprise about 10,000 ppm or less monovalent salt.
  • the aqueous base may comprise about 9,000 ppm or less monovalent salt.
  • the salt content is a result of contamination.
  • the monovalent salt typically is the type of salt found in seawater and/or salt flows.
  • the monovalent salt is sodium chloride.
  • other monovalent salts may be present. Examples of monovalent salts that may be present include, but are not necessarily limited to sodium chloride, potassium chloride, sodium bromide, potassium bromide, sodium formate, potassium formate, cesium formate and mixtures thereof.
  • the water soluble polymer is thermally stable and comprises repeat units of a first olefinic amide monomer and one or more different olefinic monomers which, in combination, make the water soluble polymer effective as a bridging agent.
  • the first olefinic amide monomer is acrylamide.
  • the water soluble polymer is a copolymer of acrylamide monomer and sulfonate monomer.
  • an advantageous sulfonate monomer is 2-acrylamido-2-methylpropane sulfonic acid or alkali metal salts thereof (“AMPS”).
  • AMPS 2-acrylamido-2-methylpropane sulfonic acid or alkali metal salts thereof
  • Preferred copolymers of acrylamide monomer and AMPS are commercially available under the name PYRO-TROL®, a trademark of Baker Hughes Incorporated.
  • the water soluble polymer is a terpolymer comprising acrylamide monomer, sulfonate monomer, and N-vinyl lactam monomer.
  • the water soluble polymers are terpolymers comprising (a) acrylamide monomer; (b) 2-acrylamido-2-methylpropane sulfonic acid or alkali metal salts thereof (“AMPS”); and (c) olefinic comonomer selected from the group consisting of acrylate monomer and N-vinyl lactam monomer.
  • AMPS 2-acrylamido-2-methylpropane sulfonic acid or alkali metal salts thereof
  • olefinic comonomer selected from the group consisting of acrylate monomer and N-vinyl lactam monomer.
  • (c) is acrylate monomer.
  • (c) is N-vinyl-2-pyrrolidone (NVP).
  • Suitable water soluble polymers generally have a 5% by weight Brookfield viscosity in freshwater of from 50 cP to 100 cP. Generally, water soluble polymers meeting this viscosity have a number average molecular weight of from about 500,000 to about 2,500,000. In one embodiment, the water soluble polymer has a number average molecular weight of from about 750,000 to about 1,500,000.
  • the drilling fluid system generally comprises from about 0.7 to about 29 kg/m 3 (0.25 lb/bbl to about 6.0 lb/bbl) water soluble polymer. In an advantageous embodiment, the drilling fluid system comprises 2.8 to about 11.5 kg/m 3 (1 to 4 lb/bbl) water soluble polymer.
  • the first olefinic monomer is derived from acrylamide monomer and has the following general structure:
  • R is a 1-alkenyl group and R 1 and R 2 independently are selected from the group consisting of hydrogen and alkyl groups having from 1 to 4 carbon atoms. In one embodiment, R 1 and R 2 are selected from the group consisting of hydrogen and methyl groups.
  • the third olefinic monomer is sulfonate monomer.
  • the sulfonate monomer has the following general structure:
  • R is selected from the group consisting of polymerizable alkenyl groups having from about 1 to about 4 carbon atoms; R 1 and R 2 are selected from the group consisting of hydrogen and methyl groups; and, X is a cation. Suitable cations are selected from the group consisting of hydrogen and alkali metal. An advantageous cation is hydrogen.
  • a preferred sulfonate is 2-acrylamido-2-methylpropanesulfonic acid (AMPS), which has the following general structure:
  • the third olefinic monomer is acrylate monomer, which has the following general structure:
  • R 1 and R 2 independently are selected from the group consisting of hydrogen and alkyl groups having from about 1 to about 4 carbon atoms; R is selected from the group consisting of hydrogen, alkyl groups having from about 1 to about 4 carbon atoms, and groups that activate the unsaturated carbon-carbon bond; and X is selected from the group consisting of hydrogen and alkali metal. In one embodiment, X is selected from the group consisting of hydrogen and sodium. In one embodiment, X is hydrogen. Examples of groups that activate the unsaturated carbon-carbon bond include, for example, groups comprising nitrogen, phosphorus, and sulfur. —N-vinyl Lactam Monomer
  • the third olefinic monomer is selected from N-vinyl lactam monomers having the following general structure:
  • R 9 , R 10 , R 11 , and R 12 independently are selected from the group consisting of hydrogen, methyl groups, and ethyl groups. In one embodiment, R 9 , R 10 , R 11 , and R 12 are the same. In one embodiment, the N-vinyl lactam monomer is N-vinyl-2-pyrrolidone (NVP), which is commercially available from a number of sources. Mole Percent of Monomers
  • the mole percent of the various monomers will vary depending upon the monomers present and other factors. The embodiments described are illustrative only.
  • the copolymer comprises less than 20 mole % sulfonate monomer. In another embodiment where the water soluble polymer is a copolymer of acrylamide monomer and sulfonate monomer, the copolymer comprises about 10 mole % or less sulfonate monomer. In an advantageous embodiment, where the water soluble polymer is a copolymer of acrylamide monomer and sulfonate monomer. In one embodiment, the water soluble polymer is a copolymer of acrylamide monomer and about 10 mole % sulfonate monomer. In one embodiment, the sulfonate monomer is AMPS.
  • the water soluble polymer is a terpolymer of acrylamide monomer/sulfonate monomer/N-vinyl lactam monomer
  • the mole percent of acrylamide monomer is from about 10 mole % to about 20 mole %
  • the mole percent of sulfonate monomer is from about 50 mole % to about 60 mole %
  • the mole percent of N-vinyl lactam monomer is from about 25 mole % to about 35 mole %.
  • the mole percent of acrylamide monomer is from about 15 mole % to about 50 mole %; the mole percent of sulfonate monomer is from about 37.5 mole % to about 55 mole %; and, the mole percent of N-vinyl lactam monomer is from about 12.5 mole % to about 30 mole %.
  • the N-vinyl lactam monomer is N-vinyl pyrrolidone (NVP).
  • the water soluble polymer is a terpolymer having a mole ratio of 55:30:15 of AMPS:NVP:acrylamide. In another embodiment, the water soluble polymer is a terpolymer having a mole ratio of 50:37.5:12.5 of acrylamide:AMPS:acrylate.
  • the water soluble polymers may be made by any suitable method include, for example, the bead method and the spray dried powder method.
  • one embodiment of the drilling fluid system further comprises a plugging agent.
  • the plugging agent is sufficiently soluble in the drilling fluid system to deform and to penetrate microfractures in the formation, which assists in sealing the formation.
  • the plugging agent assists in maintaining filtration control in the presence of contamination by monovalent salt.
  • plugging agents include, but are not necessarily limited to sized sulfonated asphalt, limestone, marble, mica, graphite, cellulosics, lignins, cellophanes, and latexes.
  • the plugging agent comprises sulfonated asphalt.
  • Sulfonated asphalts are generally produced by reacting an asphaltic material which is first mixed with a solvent followed by sulfonating the asphaltic material with a sulfonating agent.
  • Suitable solvents include alkanes. An example is hexane.
  • Suitable sulfonating agents include sulfur trioxide.
  • the sulfonation process produces asphalt-sulfonic acid, which is neutralized with a basic compound.
  • Suitable basic compounds include, for example, sodium hydroxide. See U.S. Pat. No. 4,741,868, which is incorporated herein by reference.
  • the sulfonated asphalt is in the form of a salt.
  • the sulfonated asphalt is in the form of a sodium salt or a potassium salt.
  • the plugging agent comprises a combination of sulfonated asphalt and lignite.
  • the sulfonated asphalt comprises about 20 wt. % or more lignite.
  • the sulfonated asphalt comprises about 30 wt. % or less lignite.
  • the sulfonated asphalt comprises from about 25 wt. % to about 28 wt. % lignite.
  • a suitable commercial sulfonated asphalt is SULFA-TROLL, which is commercially available from Baker Hughes Drilling Fluids.
  • the drilling fluid system advantageously comprises from about 21 to 58 kg/m 3 (7.5 to 20 lb/bbl) of plugging agent. In one embodiment, the drilling fluid system comprises about 10 lb/bbl sulfonated asphalt comprising from about 20 wt. % to about 30 wt. % lignite, based on the total weight of the plugging agent.
  • the fluid further comprises thinner. Any suitable thinner may be used.
  • the thinner comprises causticized or uncausticized lignite.
  • An exemplary commercially available lignite is LIGCO®, a trademark of Milwhite Mud Sales Company, Houston, Tex.
  • An exemplary commercially available causticized lignite is LIGCON®, a trademark of Milchem Incorporated, Houston, Tex.
  • additives may be used in the drilling fluid system.
  • additives include, but are not necessarily limited to shale stabilizer(s), other filtration control additive(s), suspending agent(s), dispersant(s), anti-balling additive(s), lubricant(s), weighting agent(s), seepage control additive(s), lost circulation additive(s), drilling enhancer(s), penetration rate enhancer(s), corrosion inhibitor(s), acid(s), base(s), buffer(s), scavenger(s), gelling agent(s), cross-linker(s), catalyst(s), soluble salts, biocides; one or more additional bridging agent, and combinations thereof.
  • the drilling fluid system may be used to drill substantially any formation. However, not all types of drilling fluid systems encounter extremely high temperatures.
  • the drilling fluid system is a drill-in or completion fluid—fluids which are more likely to be exposed to higher downhole temperatures for prolonged periods of time.
  • the drilling fluid system suitably has a density of about 9 lb/gal or more.
  • the drilling fluid system has a density of about 22 lb/gal or less.
  • Fluids were prepared using a variety of polymers from a variety of sources. The fluids were subjected to standard testing to determine rheological and fluid loss properties. HPHT was measured following the API test method described in “Recommended Practice Standard Procedure for Field Testing Water-Based Drilling Fluids,” 113B-1, 3 rd edition, incorporated herein by reference. In some instances, the method was modified as indicated in the Examples.
  • the drilling fluid system had the following general formula, where the water soluble polymer was 10 mole % AMPS polymerized with acrylamide.
  • the formula and the results are given in the following Table:
  • HPHT filtrate — 22 — 19 — 21 cm 3 /30 min pH 9.1 8.8 9.3 9.0 8.7 8.7 Without added NaCl, after 16 hours of static aging at about 232° C. (450° F.), all of the formulations measured exhibited an HPHT filtrate of 25 cm 3 /min or less after 30 minutes at about 148.9° C. (300° F.).
  • the drilling fluid system had the following general formula, where the water soluble polymer was (D) 50:37.5:12.5 mole % acrylamide:AMPS:acrylate or (E) and 55:30:15 weight % terpolymer of AMPS:NVP:acrylamide.
  • the formulas and the results are given in the following Table:
  • the drilling fluid system had the following general formula, where the water soluble polymer was (D) 50:37.5:12.5 mole % acrylamide:AMPS:acrylate.
  • the formulas and the results are given in the following Table:
  • the drilling fluid system had the following general formula, where the water soluble polymer was (D) 50:37.5:12.5 mole % acrylamide:AMPS:acrylate or (A) 10 mole % AMPS polymerized with acrylamide.
  • the formulas and the results are given in the following Table:
  • the drilling fluid system had the following general formula, where the water soluble polymer was (D) 50:37.5:12.5 mole % acrylamide:AMPS:acrylate or (A) 10 mole % AMPS polymerized with acrylamide.
  • the formulas and the results are given in the following Table:
  • the drilling fluid system had the following general formula, where the water soluble polymer was 10 mole % AMPS polymerized with acrylamide.
  • the formulas and the results are given in the following Table:
  • the drilling fluid system had the following general formula, where the water soluble polymer was (A) 10 mole % AMPS polymerized with acrylamide.
  • the formulas and the results are given in the following Table:
  • the drilling fluid system had the following general formula, where the water soluble polymer was (D) 50:37.5:12.5 mole % acrylamide:AMPS:acrylate or (A) 10 mole % AMPS polymerized with acrylamide.
  • the formulas and the results are given in the following Table:
  • the drilling fluid system had the following general formula, where the water soluble polymer was (A) 10 mole % AMPS polymerized with acrylamide; (C) 40 mole % AMPS polymerized with acrylamide; or (F) 90 weight percent NaAMPS (AMPS, sodium salt)/10 weight percent N,N-dimethylacrylamide.
  • the formulas and the results are given in the following Table:
  • the drilling fluid system had the following general formula, where the water soluble polymer was (A) 10 mole % AMPS polymerized with acrylamide.
  • the formulas and the results are given in the following Table:
  • the drilling fluid system had the following general formula, where the water soluble polymer was (A) 10 mole % AMPS polymerized with acrylamide.
  • the formulas and the results are given in the following Table:
  • the drilling fluid system had the following general formula, where the water soluble polymer was (A) 10 mole % AMPS polymerized with acrylamide.
  • the formulas and the results are given in the following Table:
  • the drilling fluid system had the following general formula, where the water soluble polymer was (A) 10 mole % AMPS polymerized with acrylamide.
  • the formulas and the results are given in the following Table:
  • Formulas 58 no added NaCl
  • Formulas 59 (10 lb/bbl SULFA-TROL® and added NaCl) exhibited an HPHT filtrate of less than 25 cm 3 /min after 30 minutes at about 177° C. (350° F.).
  • Formula 60 which contained added NaCl, but not SULFA-TROL®, exhibited an HPHT filtrate of greater than 25 cm 3 /min after 30 minutes at about 177° C. (350° F.).
  • the drilling fluid system had the following general formula, where the water soluble polymer was (A) 10 mole % AMPS polymerized with acrylamide.
  • the formulas and the results are given in the following Table:
  • Formula 63 and reaged Formula 62 which contained both NaCl and SULFA-TROL®, exhibited an HPHT filtrate of less than 25 cm 3 /min after 30 minutes at about 177° C. (350° F.). The remainder of the formulas exhibited an HPHT filtrate of greater than 25 cm 3 /min after 30 minutes or less at about 177° C. (350° F.).
  • the drilling fluid system had the following general formula, where the water soluble polymer was (A) 10 mole % AMPS polymerized with acrylamide.
  • the formulas and the results are given in the following Table:
  • Lignite has limited solubility in saline water, which may account for improved HPHT filtration control compared with SOLTEX®. It is believed that the insoluble portion of the colloidal lignite will impart particle plugging onto the filter cake, thereby slowing down filtration. SOLTEX® apparently is too soluble to impart particle plugging.
  • the drilling fluid system had the following general formula, where the water soluble polymer was (A) 10 mole % AMPS polymerized with acrylamide.
  • Each of the formulations contained 10 lb/bbl SULFA-TROL®, with varying levels of NaCl.
  • the formulas and the results are given in the following Table:

Abstract

A method and drilling fluid system for providing filtration control during drilling operations using a drilling fluid system comprising water soluble polymer comprising acrylamide monomer, the method comprising: providing a drilling fluid system having effective rheological properties, the drilling fluid system comprising aqueous base consisting essentially of freshwater, a quantity of from about 21 to 58 kg/m3 (7.5 to about 20 pounds per barrel) plugging agent, and an amount of bridging agent comprising water soluble polymer comprising acrylamide monomer which exhibits a 5% by weight Brookfield viscosity in freshwater of from about 50 cP to about 100 cP, and; contacting a subterranean formation with the drilling fluid system and maintaining effective filtration control at concentrations of about 10,000 ppm or less monovalent salt, as demonstrated in the laboratory by producing a HPHT filtrate of 25 cm3/min or less after 30 minutes at about 149° C. (300° F.) after static aging of said drilling fluid system for a period of 16 hours or more at temperatures of about 260° C. (500° F.).

Description

FIELD OF THE INVENTION
The present application relates to a method for providing filtration control during drilling operations at high temperatures. The present application also relates to water based drilling fluid systems that achieve high temperature filtration control using water soluble polymers.
BACKGROUND
Filtration control is an important property of a drilling fluid, particularly when drilling through permeable formations where the hydrostatic pressure exceeds the formation pressure. It is important for a drilling fluid to quickly form a filter cake which effectively minimizes fluid loss, but which also is thin and erodable enough to allow product to flow into the wellbore during production.
One type of filtration control additive used in water based fluids is water-soluble polymer, typically comprising acrylamide monomer. One disadvantage of water-soluble polymers is that they have limited temperature stability. As wells are drilled deeper, higher bottomhole temperatures are encountered.
Filtration control additives are needed which will quickly form a thin, erodable filter cake, and which have high temperature stability for prolonged periods of time.
BRIEF SUMMARY
The present application provides drilling fluid systems comprising water soluble polymer(s) comprising acrylamide monomer which exhibit effective rheological properties and high temperature high pressure (HTHP) filtration control at temperatures of 177° C. (350° F.) or more.
The present application provides drilling fluid systems comprising water soluble polymer comprising acrylamide monomer which exhibit effective rheological properties and HTHP filtration control at temperatures of 260° C. (500° F.) or more.
The present application provides a method for providing filtration control during drilling operations using a drilling fluid system comprising water soluble polymer comprising acrylamide monomer, the method comprising: providing a drilling fluid system having effective rheological properties, the drilling fluid system comprising aqueous base consisting essentially of freshwater, a quantity of from about 21 to 58 kg/m3 (7.5 to about 20 pounds per barrel) plugging agent, and an amount of bridging agent comprising water soluble polymer comprising acrylamide monomer which exhibits a 5% by weight Brookfield viscosity in freshwater of from about 50 cP to about 100 cP, and; contacting a subterranean formation with the drilling fluid system and maintaining effective filtration control at concentrations of about 10,000 ppm or less monovalent salt, as demonstrated in the laboratory by producing a HPHT filtrate of 25 cm3/min or less after 30 minutes at about 149° C. (300° F.) after static aging of said drilling fluid system for a period of 16 hours or more at temperatures of about 260° C. (500° F.).
The present application also provides a drilling fluid system comprising: an aqueous base consisting essentially of freshwater; a quantity of from about 21 to 58 kg/m3 (7.5 to 20 lb/bbl) plugging agent comprising sulfonated asphalt and lignite; bridging agent comprising an amount of water soluble polymer having a 5% by weight Brookfield viscosity in freshwater of from about 50 cP to about 100 cP, the water soluble polymer comprising first olefinic amide monomer copolymerized with monomer selected from the group consisting of sulfonate monomer and a combination of sulfonate monomer and N-vinyl lactam monomer, wherein the first olefinic amide monomer has the following structure:
Figure US07651980-20100126-C00001
    • wherein R is a 1-alkenyl group and R1 and R2 independently are selected from the group consisting of hydrogen and alkyl groups having from 1 to 4 carbon atoms;
the sulfonate monomer has the following structure:
Figure US07651980-20100126-C00002
    • wherein R is selected from the group consisting of polymerizable alkenyl groups having from about 1 to about 4 carbon atoms; R1 and R2 are selected from the group consisting of hydrogen and methyl groups; and, X is a cation; and,
the N-vinyl lactam monomer has the following structure:
Figure US07651980-20100126-C00003
    • wherein R9, R10, R11, and R12 independently are selected from the group consisting of hydrogen, methyl groups, and ethyl groups.
wherein, after 16 hours of static aging of the drilling fluid system at about 260° C. (500° F.), the drilling fluid system exhibits a HPHT filtrate of 25 cm3/min or less after 30 minutes at about 149° C. (300° F.).
In one embodiment, the application provides a drilling fluid system comprising: an aqueous base consisting essentially of freshwater; bridging agent comprising from about 0.7 to about 29 kg/m3 (0.25 lb/bbl to about 10.0 lb/bbl) water soluble polymer having a 5% by weight Brookfield viscosity in freshwater of from about 50 cP to about 100 cP, the water soluble polymer comprising acrylamide monomer copolymerized with monomer selected from the group consisting of sulfonate monomer and a combination of sulfonate monomer and N-vinyl lactam monomer; and, a quantity of from about 21 to 58 kg/m3 (7.5 to 20 lb/bbl) plugging agent comprising sulfonated asphalt and lignite; wherein, after 16 hours of static aging of the drilling fluid system at about 260° C. (500° F.), the drilling fluid system exhibits a HPHT filtrate of 25 cm3/min or less after 30 minutes at about 149° C. (300° F.).
In one embodiment, the application provides a drilling fluid system comprising: an aqueous base consisting essentially of freshwater; bridging agent comprising from about 0.7 to about 29 kg/m3 (0.25 lb/bbl to about 10.0 lb/bbl) water soluble polymer having a 5% by weight Brookfield viscosity in freshwater of from about 50 cP to about 100 cP, said water soluble polymer comprising monomer of acrylamide, monomer of 2-acrylamido-2-methylpropane sulfonic acid or alkali metal salts thereof, and N-vinyl pyrrolidone monomer; and, from about 21 to 58 kg/m3 (7.5 to 20 lb/bbl) plugging agent comprising sulfonated asphalt and lignite; wherein, after 16 hours of static aging of the drilling fluid system at about 260° C. (500° F.), the drilling fluid system exhibits a HPHT filtrate of 25 cm3/min or less after 30 minutes at about 149° C. (300° F.).
In another embodiment, the application provides a drilling fluid system comprising: an aqueous base consisting essentially of freshwater; bridging agent comprising from about 0.7 to about 29 kg/m3 (0.25 lb/bbl to about 10.0 lb/bbl) water soluble polymer having a 5% by weight Brookfield viscosity in freshwater of from about 50 to about 100 cP comprising monomers of acrylamide and 2-acrylamido-2-methylpropane sulfonic acid or alkali metal salts thereof; and, plugging agent comprising a quantity of from about 21 to 58 kg/m3 (7.5 to 20 lb/bbl) sulfonated asphalt comprising lignite; wherein, after 16 hours of static aging of the drilling fluid system at about 260° C. (500° F.), the drilling fluid system exhibits a HPHT filtrate of 25 cm3/min or less after 30 minutes at about 149° C. (300° F.).
DETAILED DESCRIPTION OF EMBODIMENTS
The present application provides a drilling fluid system which quickly forms a thin, erodable filter cake effective to minimize filtration of a drilling fluid system into the subterranean formation being treated. The drilling fluid system is stable for a prolonged period of time even after exposure to high temperatures. Effective filtration control is demonstrated in the laboratory when, after 16 hours of static aging at the temperature of expected exposure, the drilling fluid system exhibits a HPHT filtrate of 25 cm3/min or less after 30 minutes at about 149° C. (300° F.). In one embodiment, the drilling fluid system exhibits a HPHT filtrate of 25 cm3/min or less after 30 minutes at about 177° C. (350° F.) or more.
During drilling operations, the drilling fluid system maintains effective filtration control even after exposure to a temperature of 149° C. (300° F.) for a period of about 16 hours or more. In one embodiment, the drilling fluid system maintains effective filtration control even after exposure to a temperature of 177° C. (350° F.) for a period of about 16 hours or more. In one embodiment, the drilling fluid system maintains effective filtration control even after exposure to a temperature of 260° C. (500° F.) or more for a period of about 16 hours or more. In yet another embodiment, the drilling fluid system maintains effective filtration control even after exposure to a temperature of 287° C. (550° F.) or more for a period of about 16 hours or more.
The drilling fluid also is effective when exposed to 10,000 ppm or less monovalent salt. In one embodiment, the drilling fluid is exposed to 9,000 ppm or less monovalent salt.
The Drilling Fluid System
The drilling fluid system comprises an aqueous base, water soluble polymer, and plugging agent. The drilling fluid system also may contain other suitable components.
The Aqueous Base
In one embodiment, the aqueous base is freshwater. Although it is preferred for the aqueous base to be freshwater, the aqueous base may comprise about 10,000 ppm or less monovalent salt. In another embodiment, the aqueous base may comprise about 9,000 ppm or less monovalent salt. Typically, the salt content is a result of contamination.
Where present, the monovalent salt typically is the type of salt found in seawater and/or salt flows. Typically, the monovalent salt is sodium chloride. However, other monovalent salts may be present. Examples of monovalent salts that may be present include, but are not necessarily limited to sodium chloride, potassium chloride, sodium bromide, potassium bromide, sodium formate, potassium formate, cesium formate and mixtures thereof.
The Water Soluble Polymer
The water soluble polymer is thermally stable and comprises repeat units of a first olefinic amide monomer and one or more different olefinic monomers which, in combination, make the water soluble polymer effective as a bridging agent. In one embodiment, the first olefinic amide monomer is acrylamide. In one embodiment, the water soluble polymer is a copolymer of acrylamide monomer and sulfonate monomer. In this embodiment, an advantageous sulfonate monomer is 2-acrylamido-2-methylpropane sulfonic acid or alkali metal salts thereof (“AMPS”). Preferred copolymers of acrylamide monomer and AMPS are commercially available under the name PYRO-TROL®, a trademark of Baker Hughes Incorporated.
In another embodiment, the water soluble polymer is a terpolymer comprising acrylamide monomer, sulfonate monomer, and N-vinyl lactam monomer. In an advantageous embodiment, the water soluble polymers are terpolymers comprising (a) acrylamide monomer; (b) 2-acrylamido-2-methylpropane sulfonic acid or alkali metal salts thereof (“AMPS”); and (c) olefinic comonomer selected from the group consisting of acrylate monomer and N-vinyl lactam monomer. In one embodiment, (c) is acrylate monomer. In one embodiment, (c) is N-vinyl-2-pyrrolidone (NVP).
Suitable water soluble polymers generally have a 5% by weight Brookfield viscosity in freshwater of from 50 cP to 100 cP. Generally, water soluble polymers meeting this viscosity have a number average molecular weight of from about 500,000 to about 2,500,000. In one embodiment, the water soluble polymer has a number average molecular weight of from about 750,000 to about 1,500,000.
The drilling fluid system generally comprises from about 0.7 to about 29 kg/m3 (0.25 lb/bbl to about 6.0 lb/bbl) water soluble polymer. In an advantageous embodiment, the drilling fluid system comprises 2.8 to about 11.5 kg/m3 (1 to 4 lb/bbl) water soluble polymer.
First Olefinic Monomer
The first olefinic monomer is derived from acrylamide monomer and has the following general structure:
Figure US07651980-20100126-C00004
wherein R is a 1-alkenyl group and R1 and R2 independently are selected from the group consisting of hydrogen and alkyl groups having from 1 to 4 carbon atoms. In one embodiment, R1 and R2 are selected from the group consisting of hydrogen and methyl groups.
Sulfonate Monomer
In one embodiment, the third olefinic monomer is sulfonate monomer. In one embodiment, the sulfonate monomer has the following general structure:
Figure US07651980-20100126-C00005
wherein R is selected from the group consisting of polymerizable alkenyl groups having from about 1 to about 4 carbon atoms; R1 and R2 are selected from the group consisting of hydrogen and methyl groups; and, X is a cation. Suitable cations are selected from the group consisting of hydrogen and alkali metal. An advantageous cation is hydrogen.
A preferred sulfonate is 2-acrylamido-2-methylpropanesulfonic acid (AMPS), which has the following general structure:
Figure US07651980-20100126-C00006
The Third Olefinic Monomer
In one embodiment, the third olefinic monomer is acrylate monomer, which has the following general structure:
Figure US07651980-20100126-C00007
wherein R1 and R2 independently are selected from the group consisting of hydrogen and alkyl groups having from about 1 to about 4 carbon atoms; R is selected from the group consisting of hydrogen, alkyl groups having from about 1 to about 4 carbon atoms, and groups that activate the unsaturated carbon-carbon bond; and X is selected from the group consisting of hydrogen and alkali metal. In one embodiment, X is selected from the group consisting of hydrogen and sodium. In one embodiment, X is hydrogen. Examples of groups that activate the unsaturated carbon-carbon bond include, for example, groups comprising nitrogen, phosphorus, and sulfur.
—N-vinyl Lactam Monomer
In another embodiment, the third olefinic monomer is selected from N-vinyl lactam monomers having the following general structure:
Figure US07651980-20100126-C00008
wherein R9, R10, R11, and R12 independently are selected from the group consisting of hydrogen, methyl groups, and ethyl groups. In one embodiment, R9, R10, R11, and R12 are the same. In one embodiment, the N-vinyl lactam monomer is N-vinyl-2-pyrrolidone (NVP), which is commercially available from a number of sources.
Mole Percent of Monomers
The mole percent of the various monomers will vary depending upon the monomers present and other factors. The embodiments described are illustrative only.
Where the water soluble polymer is a copolymer of acrylamide monomer and sulfonate monomer, the copolymer comprises less than 20 mole % sulfonate monomer. In another embodiment where the water soluble polymer is a copolymer of acrylamide monomer and sulfonate monomer, the copolymer comprises about 10 mole % or less sulfonate monomer. In an advantageous embodiment, where the water soluble polymer is a copolymer of acrylamide monomer and sulfonate monomer. In one embodiment, the water soluble polymer is a copolymer of acrylamide monomer and about 10 mole % sulfonate monomer. In one embodiment, the sulfonate monomer is AMPS.
Where the water soluble polymer is a terpolymer of acrylamide monomer/sulfonate monomer/N-vinyl lactam monomer, the mole percent of acrylamide monomer is from about 10 mole % to about 20 mole %; the mole percent of sulfonate monomer is from about 50 mole % to about 60 mole %; and, the mole percent of N-vinyl lactam monomer is from about 25 mole % to about 35 mole %. In one embodiment, the mole percent of acrylamide monomer is from about 15 mole % to about 50 mole %; the mole percent of sulfonate monomer is from about 37.5 mole % to about 55 mole %; and, the mole percent of N-vinyl lactam monomer is from about 12.5 mole % to about 30 mole %. In one embodiment having the foregoing percentage composition, the N-vinyl lactam monomer is N-vinyl pyrrolidone (NVP).
In one embodiment, the water soluble polymer is a terpolymer having a mole ratio of 55:30:15 of AMPS:NVP:acrylamide. In another embodiment, the water soluble polymer is a terpolymer having a mole ratio of 50:37.5:12.5 of acrylamide:AMPS:acrylate.
The water soluble polymers may be made by any suitable method include, for example, the bead method and the spray dried powder method.
The Plugging Agent
In order to assist in forming an effective seal for filtration control, one embodiment of the drilling fluid system further comprises a plugging agent. The plugging agent is sufficiently soluble in the drilling fluid system to deform and to penetrate microfractures in the formation, which assists in sealing the formation. The plugging agent assists in maintaining filtration control in the presence of contamination by monovalent salt.
Examples of suitable plugging agents include, but are not necessarily limited to sized sulfonated asphalt, limestone, marble, mica, graphite, cellulosics, lignins, cellophanes, and latexes. In one embodiment, the plugging agent comprises sulfonated asphalt.
Sulfonated asphalts are generally produced by reacting an asphaltic material which is first mixed with a solvent followed by sulfonating the asphaltic material with a sulfonating agent. Suitable solvents include alkanes. An example is hexane. Suitable sulfonating agents include sulfur trioxide. The sulfonation process produces asphalt-sulfonic acid, which is neutralized with a basic compound. Suitable basic compounds include, for example, sodium hydroxide. See U.S. Pat. No. 4,741,868, which is incorporated herein by reference. In one embodiment, the sulfonated asphalt is in the form of a salt. In one embodiment, the sulfonated asphalt is in the form of a sodium salt or a potassium salt.
In an advantageous embodiment, the plugging agent comprises a combination of sulfonated asphalt and lignite. In one embodiment, the sulfonated asphalt comprises about 20 wt. % or more lignite. Suitably, the sulfonated asphalt comprises about 30 wt. % or less lignite. In a particularly advantageous embodiment, the sulfonated asphalt comprises from about 25 wt. % to about 28 wt. % lignite. A suitable commercial sulfonated asphalt is SULFA-TROLL, which is commercially available from Baker Hughes Drilling Fluids.
In one embodiment, the drilling fluid system advantageously comprises from about 21 to 58 kg/m3 (7.5 to 20 lb/bbl) of plugging agent. In one embodiment, the drilling fluid system comprises about 10 lb/bbl sulfonated asphalt comprising from about 20 wt. % to about 30 wt. % lignite, based on the total weight of the plugging agent.
In one embodiment, the fluid further comprises thinner. Any suitable thinner may be used. In one embodiment, the thinner comprises causticized or uncausticized lignite. An exemplary commercially available lignite is LIGCO®, a trademark of Milwhite Mud Sales Company, Houston, Tex. An exemplary commercially available causticized lignite is LIGCON®, a trademark of Milchem Incorporated, Houston, Tex.
Other additives may be used in the drilling fluid system. Such additives include, but are not necessarily limited to shale stabilizer(s), other filtration control additive(s), suspending agent(s), dispersant(s), anti-balling additive(s), lubricant(s), weighting agent(s), seepage control additive(s), lost circulation additive(s), drilling enhancer(s), penetration rate enhancer(s), corrosion inhibitor(s), acid(s), base(s), buffer(s), scavenger(s), gelling agent(s), cross-linker(s), catalyst(s), soluble salts, biocides; one or more additional bridging agent, and combinations thereof.
The drilling fluid system may be used to drill substantially any formation. However, not all types of drilling fluid systems encounter extremely high temperatures. In one embodiment, the drilling fluid system is a drill-in or completion fluid—fluids which are more likely to be exposed to higher downhole temperatures for prolonged periods of time.
The drilling fluid system suitably has a density of about 9 lb/gal or more. Suitably, the drilling fluid system has a density of about 22 lb/gal or less.
The application will be better understood with reference to the following Examples which are for purposes of illustration only:
Procedures
Fluids were prepared using a variety of polymers from a variety of sources. The fluids were subjected to standard testing to determine rheological and fluid loss properties. HPHT was measured following the API test method described in “Recommended Practice Standard Procedure for Field Testing Water-Based Drilling Fluids,” 113B-1, 3rd edition, incorporated herein by reference. In some instances, the method was modified as indicated in the Examples.
In the following formulations, the Experimental Water Soluble Polymers from various sources and batches had the following monomeric content:
    • A. 10 mole % AMPS polymerized with acrylamide;
    • B. 20 mole % AMPS/acrylamide;
    • C. 40 mole % AMPS:acrylamde;
    • D. 50:37.5:12.5 mole % acrylamide:AMPS: acrylate terpolymer;
    • E. 55:30:15 mole % terpolymer of AMPS:NVP:acrylamide; and,
    • F. 90 weight percent NaAMPS (AMPS, sodium salt)/10 weight percent N,N-dimethylacrylamide
      A number of commercial products are used in the formulations described in the examples. The following is a description of these products and their sources:
      Products Available from Baker Hushes Drilling Fluids:
    • MIL-GEL™ is a ground montmorillonite used to simulate formation shale contaminant;
    • MILGEL-NT™ is a ground montmorillonite used to simulate formation shale contaminant;
    • CHEMTROL®-X is a blend of ground lignitic earth and synthetic maleic anhydride copolymers;
    • MIL-TEMP® is a maleic anhydride copolymer useful to prevent thermal degradation of a drilling fluid system;
    • MIL-CARB® and MIL-CARB® 5 are products comprising ground marble or calcium carbonate particles;
    • MIL-BAR® is a barite additive;
    • DFE-129™ is an acrylamide/AMPS copolymer;
    • CHEK-LOSS® PLUS is a water-insoluble, ultra-fine, (lignin) material used for controlling seepage and loss of circulation while drilling through depleted or under-pressured zones;
    • SULFA-TROL® is a sulfonated asphalt;
    • MAX-TROL® is a sulfonated resin additive for water-based mud systems;
    • KEM-SEAL® PLUS is a water soluble polymer having about 90 wt. % NaAMPS (AMPS, sodium salt) and 10 wt. % N,N-dimethylacrylamide;
    • ALL-TEMP® is an acrylate tetrapolymer.
    • LIGCON® is causticized lignite;
    • LIGCO® is lignite;
    • PROTECTO-MAGIC™ is a ground asphalt.
      Products Available from Other Commercial Sources:
    • REV-DUST is a simulated drilled product which may be obtained from Mil-White Company, Houston, Tex.;
    • POLYDRILL® is an anionic synthetic polymer commercially available from Degussa Construction Polymers GMBH Corporation, Fed. Rep. Germany;
    • BORE-DRILL™ is an anionic synthetic polymer commercially available from Borden Chemicals;
    • SOLTEX® is a sulfonated asphalt, commercially available from Chevron Phillips Chemical Company;
    • DRISCAL D is a water soluble polymer provided by Drilling Specialties Company.
      In a number of the examples, POLYDRILL® or another component is listed twice in order to show a difference in order of addition while mixing
The application will be better understood with reference to the following examples, which are illustrative only:
EXAMPLE 1
In the following Example, the drilling fluid system had the following general formula, where the water soluble polymer was 10 mole % AMPS polymerized with acrylamide. The formula and the results are given in the following Table:
Experimental Water Soluble Polymer
A A A
Freshwater, ml (lb) 239 239 239
(0.68) (0.68) (0.68)
MILGEL ™ NT, kg (lb) 4.5 4.5 4.5
(10.0) (10.0) (10.0)
CHEMTROL ® X, kg (lb) 4.5 4.5 4.5
(10.0) (10.0) (10.0)
Caustic Soda, kg (lb) 0.23 0.23 0.23
(0.5) (0.5) (0.5)
MIL-TEMP ®, kg (lb) 0.9 0.9 0.9
(2.0) (2.0) (2.0)
10 mole % AMPS polymerized 0.9 0.9 0.9
with acrylamide, kg (lb) (2.0) (2.0) (2.0)
MIL-CARB ®, kg (lb) 4.5 4.5 4.5
(10.0) (10.0) (10.0)
MIL-CARB ® 5, kg (lb) 2.3 2.3 2.3
(5.0) (5.0) (5.0)
MIL-BAR ®, kg (lb) 182.7 182.7 182.7
(403.0) (403.0) (403.0)
FLUID PROPERTIES
Fann 35 at 49° C. (120° F.)
232° C. 232° C. 232° C.
(450° F.) (450° F.) (450° F.)
Static Age Static Age Static Age
Initial 16 Hours Initial 16 Hours Initial 16 Hours
600 rpm 90 147 72 142 69 140
300 rpm 50 87 39 83 38 82
200 rpm 36 64 28 60 28 61
100 rpm 22 39 12 37 12 38
 6 rpm 5 9 5 8 5 9
 3 rpm 4 7 4 6 4 7
Plastic Viscosity, cP 40 60 33 59 31 58
Yield Point, Pa 4.8 12.9 2.9 11.5 3.4 11.5
(lb/100 ft2) (10) (27) (6) (24) (7) (24)
Gels, Pa 2.9/3.4 4.3/16.3 2.4/3.4 3.8/9.58 2.4/3.4 4.3/11
(lb/100 ft2) (6/7) (9/34) (5/7) (8/20) (5/7) (9/23)
API fluid loss, cm3/30 min 2.0 2.3 2.1 2.5 2.4 3.0
300° F. HPHT filtrate, — 22 — 19 — 21
cm3/30 min
pH 9.1 8.8 9.3 9.0 8.7 8.7

Without added NaCl, after 16 hours of static aging at about 232° C. (450° F.), all of the formulations measured exhibited an HPHT filtrate of 25 cm3/min or less after 30 minutes at about 148.9° C. (300° F.).
EXAMPLE 2
In the following test, the drilling fluid system had the following general formula, where the water soluble polymer was (D) 50:37.5:12.5 mole % acrylamide:AMPS:acrylate or (E) and 55:30:15 weight % terpolymer of AMPS:NVP:acrylamide. The formulas and the results are given in the following Table:
Form.
1 2 3 4 5 6
Experimental Water Soluble Polymer
D E D E D E
Fresh- 0.07 0.07 0.07 0.07 0.07 0.07
water, m3 (0.56) (0.56) (0.56) (0.56) (0.56) (0.56)
(bbl)
MIL- 2.3 2.3 2.3 2.3 1.8 1.8
GEL ™, (5.0) (5.0) (5.0) (5.0) (4.0) (4.0)
kg (lb)
MIL- 0.7 0.7 0.7 0.7 1.1 1.1
TEMP ®, (1.5) (1.5) (1.5) (1.5) (2.5) (2.5)
kg (lb)
CHEM- 2.7 2.7 2.7 2.7 2.3 2.3
TROL ® X, (6.0) (6.0) (6.0) (6.0) (5.0) (5.0)
kg (lb)
Caustic 0.2 0.2 0.2 0.2 0.2 0.2
soda, (0.5) (0.5) (0.5) (0.5) (0.5) (0.5)
kg (lb)
KEM- 0.5 0.5 0.5 0.5 0.5 0.5
SEAL ® (1.0) (1.0) (1.0) (1.0) (0.5) (0.5)
PLUS,
kg (lb)
Experimental 0.9 0.9 0.9 0.9 0.9 0.9
water (2.0) (2.0) (2.0) (2.0) (2.0) (2.0)
soluble
polymer,
kg (lb)
POLY- 3.6 3.6 3.6 3.6 3.2 3.2
DRILL ™, (8.0) (8.0) (8.0) (8.0) (7.0) (7.0)
lb (kg)
MIL- 4.5 4.5 4.5 4.5 4.5 4.5
CARB ®, (10) (10) (10) (10) (10) (10)
kg (lb)
MIL- 248.4 248.4 248.4 248.4 248.4 248.4
BAR ®, (547.7) (547.7) (547.7) (547.7) (547.7) (547.7)
kg (lb)
Form.
1 2 3 4 5 6
FLUID PROPERTIES Fann 35 at 49° C. (120° F.)
204° C. 204° C. 260° C. 260° C. 260° C. 260° C.
(400° F.) (400° F.) (500° F.) (500° F.) (500° F.) (500° F.)
Static Static Static Static Static Static
Age Age Age Age Age Age
16 16 16 16 16 16
Initial Hours Initial Hours Initial Hours Initial Hours Initial Hours Initial Hours
600 rpm 124 119 188 153 131 >300 108 100 161 237
300 rpm 68 82 107 104 108 >300 57 69 92 196
200 rpm 49 69 77 87 100 >300 40 60 66 185
100 rpm 29 52 45 65 88 >300 23 48 37 161
 6 rpm 6 29 7 32 71 265 5 30 5 125
 3 rpm 4 29 5 32 70 240 4 27 3 122
Plastic 56 37 81 49 23 NM* 51 31 69 41
Viscosity,
cP
Yield 5.7 23.5 12.5 26.3 40.7 NM* 2.9 18.2 6.2 72.3
Point, Pa (12) (45) (26) (55) (85) (6) (38) (23) (155)
(lb/100 ft2)
Gels, Pa 2.4/4.3 17.2/28.7 2.9/5.2 21.1/35.9 39.7/56 96.7/98.2 2.4/3.3 16.3/32.6 2.4/4.3 59.4/60
(lb/100 ft2) (5/9) (36/60) (6/11) (44/75) (83/117) (202/205) (5/8) (34/68) (5/9) (124/125)
API fluid 1.4 1.9 1.8 1.8 2.6 — 1.8 3.0 1.3 4.6
loss,
cm3/30 min
177° C. — 6.0 — 11 <1† — — 16 — —
(350° F.)
HPHT
filtrate,
cm3/30 min
pH 9.5 8.8 9.5 8.7 8.4 — 9.5 8.4 9.6 8.5
†Possible plugged valve stem during HPHT filtration
*Non measurable.

Without added NaCl, after 16 hours of static aging at about 204° C. (400° F.) for Formulas 1 and 2 and at 260° C. (500° F.) for Formulas 3-6, all of the formulations for which HPHT filtrate was measured exhibited an HPHT filtrate of 25 cm3/min or less after 30 minutes at about 177° C. (350° F.). The yield points were more variable than desired, so further study was undertaken to determine how to stabilize the yield point, among other things.
EXAMPLE 3
In the following test, the drilling fluid system had the following general formula, where the water soluble polymer was (D) 50:37.5:12.5 mole % acrylamide:AMPS:acrylate. The formulas and the results are given in the following Table:
Form.
7 8 9 10 11 12
Experimental Water Soluble Polymer
D D D D D D
Fresh- 196 196 196 196 196 196
water, (0.56) (0.56) (0.56) (0.56) (0.56) (0.56)
ml(bbl)
MIL- 1.4 1.6 1.4 2.3 1.4 1.4
GEL ™, (3.0) (3.5) (3.0) (4.0) (3.0) (3.0)
kg (lb)
MIL- 0.9 0.9 1.1 1.1 0.9 0.9
TEMP ®, (2.0) (2.0) (2.5) (2.5) (2.0) (2.0)
kg (lb)
CHEM- 2.3 2.3 1.1 2.3 2.3 2.3
TROL ® X, (5.0) (5.0) (2.5) (5.0) (5.0) (5.0)
kg (lb)
Caustic 0.2 0.2 0.2 0.2 0.2 0.2
soda, (0.5) (0.5) (0.5) (0.5) (0.5) (0.5)
kg (lb)
KEM- — 0.2 0.2 — — 0.2
SEAL ® (0.5) (0.5) (0.5)
PLUS,
kg (lb)
Experimental 1.1 1.1 1.1 0.9 1.4 0.9
Water (2.5) (2.5) (2.5) (2.0) (3.0) (2.0)
soluble
polymer,
kg (lb)
POLY- 3 3 3 3 2.3 1.6
DRILL ™, (7.0) (7.0) (7.0) (7.0) (5.0) (3.5)
kg (lb)
MIL- 2.3 2.3 2.3 4.5 4.5 4.5
CARB ®, (5.0) (5.0) (5.0) (10) (10) (10)
kg (lb)
MIL- 248.4 248.4 248.4 248.4 248.4 248.4
BAR ®, (547.7) (547.7) (547.7) (547.7) (547.7) (547.7)
kg (lb)
Form.
7 8 9 10 11 12
FLUID PROPERTIES Fann 35 at 49° C. (120° F.)
260° C.) 260° C. 260° C. 260° C. 260° C. 260° C.
500° F.) (500° F.) (500° F.) (500° F.) (500° F.) (500° F.)
Static Static Static Static Static Static
Age 16 Age 16 Age 16 Age 16 Age 16 Age 16
Initial Hours Initial Hours Initial Hours Initial Hours Initial Hours Initial Hours
600 rpm 76 85 103 80 104 69 78 96 89 70 118 81
300 rpm 39 52 53 49 54 44 39 59 45 44 60 41
200 rpm 27 41 38 37 38 34 27 47 33 33 42 26
100 rpm 15 29 21 26 21 24 15 34 19 22 24 13
 6 rpm 3 14 4 13 4 11 3 20 4 9 4 2
 3 rpm 2 12 3 13 3 10 2 19 3 9 3 1
Plastic 37 33 50 31 50 25 39 37 34 26 58 40
Viscosity,
cP
Yield 0.96 9.1 1.4 8.6 1.9 9.1 0 10.5 5.3 8.6 8.6 0.48
Point, (2) (19) (3) (18) (4) (19) (0) (22) (11) (18) (18) (1)
Pa
(lb/100 ft2)
Gels, 1.4/2.9 8.6/18.2 2.4/2.9 10/19.6 2.4/3.4 8.1/14.8 1.9/2.9 13.9/33 1.9/3.4 7.7/18.7 2.5/3.4 .96/7.7
Pa(lb/100 ft2) (3/6) (18/38) (5/6) (21/41) (5/7) (17/31) (4/6) (29/69) (4/7) (16/39) (5/7) (2/16)
API fluid 2.5 3.0 1.6 2.6 2.7 4.0 1.9 2.6 3.0 3.2 2.5 2.6
loss,
cm3/30 min
177° C. — *80 — *50 — — — — — 50 — 50
(350° F.) (6 min) (26 min)
HPHT
filtrate,
cm3/30 min
pH 9.7 8.2 9.5 8.3 9.5 8.3 9.5 8.6 9.5 8.6 9.6 8.5

Surprisingly, even in the absence of added NaCl, after 16 hours of static aging at about 260° C. (500° F.), all of the formulations for which HPHT filtrate was measured exhibited an HPHT filtrate of greater than 25 cm3/min after 30 minutes or less at about 177° C. (350° F.). The results are believed to be attributable to variability in the properties of the commercially available polymer.
EXAMPLE 4
In the following test, the drilling fluid system had the following general formula, where the water soluble polymer was (D) 50:37.5:12.5 mole % acrylamide:AMPS:acrylate or (A) 10 mole % AMPS polymerized with acrylamide. The formulas and the results are given in the following Table:
Formulation
13 14 15 16 17
Experimental Water Soluble Polymer
D D A A D
Freshwater, 196 196 176 196 196
ml(bbl) (0.56) (0.56) (0.50) (0.50) (0.56)
MIL-GEL ™, 1.4 1.4 2.3 2.3 2.3
kg (lb) (3.0) (3.0) (4.0) (4.0) (4.0)
MIL-TEMP ®, 0.9 0.9 1.1 1.1 1.1
kg (lb) (2.0) (2.0) (2.5) (2.5) (2.5)
CHEM-TROL ® 2.3 2.3 2.3 2.3 1.1
X, kg (lb) (5.0) (5.0) (5.0) (5.0) (2.5)
Caustic soda, 0.23 0.23 0.23 0.23 —
kg (lb) (0.5) (0.5) (0.5) (0.5)
KEM-SEAL ® 0.5 0.5 0.23 0.23 0.23
PLUS, kg (lb) (1.0) (1.0) (0.5) (0.5) (0.5)
Experimental 0.9 0.9 0.9 0.9 0.9
Water soluble (2.0) (2.0) (2.0) (2.0) (2.0)
polymer, kg (lb)
MAX-TROL ®, 1.6 — — — —
kg (lb) (3.5)
POLYDRILL ™, — — 3.2 3.2 4
kg (lb) (7.0) (7.0) (9.0)
BOREDRILL ™, — 1.6 — — —
kg (lb) (3.5)
MIL-CARB ®, 4.5 4.5 4.5 4.5 4.5
kg (lb) (10) (10) (10) (10) (10)
MIL-BAR ®, 248.4 248.4 248.4 248.4 248.4
kg (lb) (547.7) (547.7) (547.7) (547.7) (547.7)
Caustic soda, — — — — Adj. pH to 9.0
kg (lb)
Formulation
13 14 15 16 17
FLUID PROPERTIES Fann 35 at 49° C. (120° F.)
260° C. 260° C. 260° C. 260° C. 260° C.
(500° F.) (500° F.) (500° F.) (500° F.) (500° F.)
Static Static Static Static Static
Age 16 Age 16 Age 16 Age 16 Age 16
Initial Hours Initial Hours Initial Hours Initial Hours Initial Hours
600 rpm 117 71 166 164 233 85 279 123 116 72
300 rpm 58 35 89 96 127 47 156 72 66 47
200 rpm 40 24 62 72 91 35 117 54 47 37
100 rpm 22 14 34 45 53 23 68 35 27 27
 6 rpm 4 2 5 8 9 8 12 10 5 13
 3 rpm 2 2 3 6 7 6 9 8 3 11
Plastic Viscosity, 59 36 77 68 106 38 123 51 50 25
Cp
Yield Point, −0.47 −0.47 5.7 13.4 10 4.3 15.8 10 7.7 10.5
Pa(lb/100 ft2) (−1) (−1) (12) (28) (21) (9) (33) (21) (16) (22)
Gels, Pa 1.9/2. 2.4/8.1 2.4/3 7.7/23 4.8/9.6 6.2/17.7 6.2/12 7.7/19. 2.4/8.6 8.6/21
(lb/100 ft2) (4/5) (5/17) (5/6) (16/48) (10/20) (13/37) (13/26) (16/40) (5/18) (18/45)
API fluid loss, 2.4 8.2 2.8 >10 2.6 2.2 2.6 2.6 1.8 3.5
cm3/30 min
177° C. (350° F.) — — — — — NC — >50 — 35
HPHT filtrate,
cm3/30 min
pH 9.9 8.3 9.9 8.1 9.0 8.2 9.0 8.3 9.0 8.2

Surprisingly, even in the absence of added NaCl, after 16 hours of static aging at about 260° C. (500° F.), all of the formulations for which HPHT filtrate was measured exhibited an HPHT filtrate of greater than 25 cm3/min after 30 minutes or less at about 177° C. (350° F.). The results are believed to be attributable to variability in the properties of the commercially available polymer.
EXAMPLE 5
In the following test, the drilling fluid system had the following general formula, where the water soluble polymer was (D) 50:37.5:12.5 mole % acrylamide:AMPS:acrylate or (A) 10 mole % AMPS polymerized with acrylamide. The formulas and the results are given in the following Table:
Formulation
18 19 20 21 22
Experimental water soluble polymer
D D A A A
Freshwater, ml 196 196 196 196 196
(bbl) (0.56) (0.56) (0.56) (0.56) (0.56)
MIL-GEL ™, 2.3 2.3 2.3 2.3 2.3
kg (lb) (4.0) (4.0) (5.0) (5.0) (5.0)
MIL-TEMP ®, kg 1.1 1.1 0.7 0.7 0.7
(lb) (2.5) (2.5) (1.5) (1.5) (1.5)
CHEM-TROL ® X, 3.2 1.6 2.7 2.7 2.7
kg (lb) (7.0) (3.5) (6.0) (6.0) (6.0)
Caustic soda, — — 0.23 0.23 0.23
kg (lb) (0.5) (0.5) (0.5)
KEM- 0.5 0.5 0.5 0.5 0.5
SEAL ® PLUS, (1.0) (1.0) (1.0) (1.0) (1.0)
kg (lb)
Experimental 1.1 1.1 0.9 0.9 0.9
Water Soluble (2.5) (2.5) (2.0) (2.0) (2.0)
Polymer, kg (lb)
MAX-TROL ®, — — — — —
kg (lb)
POLYDRILL ™, 1.6 3.2 3.6 3.6 3.6
kg (lb) (3.5) (7.0) (8.0) (8.0) (8.0)
BOREDRILL ™, — — — — —
kg (lb)
MIL-CARB ®, 4.5 4.5 4.5 4.5 4.5
kg (lb) (10) (10) (10) (10) (10)
MIL-BAR ®, 248.4 248.4 248.4 248.4 248.4
kg (lb) (547.7) (547.7) (547.7) (547.7) (547.7)
Caustic soda, Adj. pH to 9.0 Adj. pH to 9.0 — — —
kg (lb)
Formulation
18 19 20 21 22
FLUID PROPERTIES Fann 35 at 49° C. (120° F.)
260° C. 260° C. 260° C. 260° C. 260° C.
(500° F.) (500° F.) (500° F.) (500° F.) (500° F.)
Static Static Static Static Static
Age 16 Age 16 Age 16 Age 16 Age 16
Initial Hours Initial Hours Initial Hours Initial Hours Initial Hours
600 rpm 168 66 223 112 224 131
300 rpm 92 38 123 67 131 88
200 rpm 66 26 87 52 93 73
100 rpm 38 16 50 37 54 55
 6 rpm 7 3 9 15 9 32
 3 rpm 4 2 6 15 7 32
Plastic Viscosity, 76 28 101 45 93 43
Cp
Yield Point, 7.7 4.8 10 10.5 18.2 21.5
Pa(lb/100 ft2) (16) (10) (21) (22) (38) (45)
Gels, 2.9/4.3 3.8/11.5 3.8/6.2— 12/30.6 4.3/7.2 21.5/39
Pa (lb/100 ft2) (6/9) (8/24) (8/13) (25/64) (9/15) (45/82)
API fluid loss, 2.5 3.4 0.9 1.8 1.7 2.2
cm3/30 min
177° C. (350° F.) — 76 — 22 — 14
HPHT filtrate,
cm3/30 min
pH 9.0 8.2 9.8 9.0 9.8 8.5

After 16 hours of static aging at about 260° C. (500° F.), Formula 19 exhibited an HPHT filtrate of greater than 25 cm3/min after 30 minutes or less at about 177° C. (350° F.), and Formulas 21 and 22 exhibited an HPHT filtrate of less than 25 cm3/min after 30 minutes at about 177° C. (350° F.). The negative results for Formula 19 are believed to be attributable to variability in the properties of the commercially available polymer.
EXAMPLE 6
In the following test, the drilling fluid system had the following general formula, where the water soluble polymer was 10 mole % AMPS polymerized with acrylamide. The formulas and the results are given in the following Table:
Form.
21 (con't) 22 (con't) 23 24
Experimental Water Soluble Polymer
A A A A
Freshwater, 196 196 196 176
ml(bbl) (0.56) (0.56) (0.56) (0.50)
MIL-GEL ™, 2.3 2.3 2.3 2.3
kg (lb) (5.0) (5.0) (5.0) (5.0)
MIL-TEMP ®, 0.7 0.7 0.7 0.7
kg (lb) (1.5) (1.5) (1.5) (1.5)
CHEM- 2.7 2.7 2.7 2.7
TROL ® X, (6.0) (6.0) (6.0) (6.0)
kg (lb)
Caustic soda, 0.23 0.23 0.23 0.23
kg (lb) (0.5) (0.5) (0.5) (0.5)
KEM- 0.5 0.5 0.5 0.5
SEAL ® PLUS, (1.0) (1.0) (1.0) (1.0)
kg (lb)
Experimental 0.9 0.9 0.9 0.9
Water (2.0) (2.0) (2.0) (2.0)
Soluble
Polymer,
kg (lb)
POLY- 3.6 3.6 3.6 3.6
(8.0) (8.0) (8.0) (8.0)
DRILL ™,
kg (lb)
MIL-CARB ®, 4.5 4.5 4.5 4.5
kg (lb) (10) (10) (10) (10)
MIL-BAR ®, 248.4 248.4 248.4 248.4
kg (lb) (547.7) (547.7) (547.7) (547.7)
Caustic soda, — — — —
kg (lb)
Form.
21 (con't) 22 (con't) 23 24
FLUID PROPERTIES Fann 35 at 49° C. (120° F.)
260° C. 260° C. 260° C. 260° C. 260° C. 260° C. 260° C. 260° C.
(500° F.) (500° F.) (500° F.) (500° F.) (500° F.) (500° F.) (500° F.) (500° F.)
Static Static Static Static Static Static Static Static
Age 48 Age 72 Age 48 Age 72 Age 16 Age 48 Age 72 Age 16
Hours Hours Hours Hours Initial Hours Hours Hours Initial Hours
600 rpm 113 103 169 105 243 124 109 100 >300 96
300 rpm 62 54 111 64 134 79 63 50 226 76
200 rpm 45 39 90 49 96 65 47 35 169 68
100 rpm 28 23 67 34 55 48 30 21 115 55
 6 rpm 9 5 38 14 8 26 9 4 25 40
 3 rpm 9 4 38 14 6 27 7 3 21 40
Plastic 51 49 58 41 109 45 46 50 NM 20
Viscosity, Cp
Yield Point, 5.2 2.4 25.4 11 12 16.3 8.1 0 NM 26.8
Pa(lb/100 ft2) (11) (5) (53) (23) (25) (34) (17) (0) (56)
Gels, Pa 7.7/21.5 4.8/14.8 24.9/45.4 12/25.3 3.8/5.7 18.2/36.4 8.6/21.5 4.3/14.8 13.9/28.7 23/35.4
(lb/100 ft2) (16/45) (10/31) (52/95) (25/53) (8/12) (38/76) (18/45) (9/31) (29/60) (48/74)
API fluid 2.8 2.2 2.6 2.2 1.0 1.9 2.0 2.2 3.0 2.4
loss,
cm3/30 min
177° C. (350° F.) 52 — 31 16 — 21 16 16 — 15
HPHT (14 min)
filtrate,
cm3/30 min
pH 8.8 8.6 8.7 8.6 9.4 8.5 8.4 8.4 6.6 9.2
Settling None

After 16 hours of static aging at about 260° C. (500° F.), Formulas 21 and 22 exhibited an HPHT filtrate of greater than 25 cm3/min after 30 minutes or less at about 177° C. (350° F.), and Formulas 23 and 24 exhibited an HPHT filtrate of less than 25 cm3/min after 30 minutes at about 177° C. (350° F.). The result was believed to be attributable to variability among commercially available polymers.
EXAMPLE 7
In the following test, the drilling fluid system had the following general formula, where the water soluble polymer was (A) 10 mole % AMPS polymerized with acrylamide. The formulas and the results are given in the following Table:
Formulation
25 26 27 28
Experimental Water Soluble Polymer
A A A A
Freshwater, 176 176 196 196
ml(bbl) (0.50) (0.50) (0.56) (0.56)
MIL-GEL ™, 2.3 2.3 2.3 2.3
kg (lb) (5.0) (5.0) (4.0) (4.0)
MIL-TEMP ®, 0.7 0.7 0.9 0.9
kg (lb) (1.5) (1.5) (2.0) (2.0)
CHEM- 2.7 2.7 2.3 3.6
TROL ®
X, kg (lb) (6.0) (6.0) (5.0) (8.0)
Caustic soda, 0.23 0.23 0.23 0.34
kg (lb) (0.5) (0.5) (0.5) (0.75)
KEM- 0.5 0.5 0.5 0.5
SEAL ®  (1.0) (1.0) (1.0) (1.0)
PLUS, kg (lb)
Experimental 0.9 0.9 0.9 0.9
Water Soluble (2.0) (2.0) (2.0) (2.0)
Polymer,
kg (lb)
MAX- — — — —
TROL ®,
kg (lb)
POLYDRILL ™, 3.6 3.6 3.2 2.3
kg (lb) (8.0) (8.0) (7.0) (5.0)
BOREDRILL ™, — — — —
kg (lb)
MIL-CARB ®, 4.5 4.5 4.5 4.5
kg (lb) (10) (10) (10) (10)
MIL-BAR ®, 248.4 248.4 248.4 248.4
kg (lb) (547.7) (547.7) (547.7) (547.7)
Caustic soda, — — — —
kg (lb)
Formulation
25 26 27 28
FLUID PROPERTIES Fann 35 at 49° C. (120° F.)
260° C.
(500° 260° C. 260° C. 260° C. 260° C. 260° C. 260° C. 260° C.
F.) (500° F.) (500° F.) (500° F.) (500° F.) (500° F.) (500° F.) (500° F.)
Static Static Static Static Static Static Static Static
Age 16 Age 16 Age 48 Age 72 Age 16 Age 48 Age 72 Age 16
Initial Hours Initial Hours Hours Hours Initial Hours Hours Hours Initial Hours
600 rpm >300 >300 >300 80 65 47 191 85 92 79 202 92
300 rpm 242 249 238 46 32 25 100 50 41 41 106 56
200 rpm 176 221 180 36 23 15 70 35 29 26 74 42
100 rpm 105 183 113 25 14 9 40 21 16 14 41 27
 6 rpm 20 124 26 12 5 2 6 4 3 2 6 9
 3 rpm 16 122 22 12 4 1 4 4 2 1 4 9
Plastic NM NM NM 34 33 22 91 35 51 38 96 36
Viscosity,
cP
Yield NM NM NM 5.7 −0.48 1.4 4.3 7.2 −4.8 1.4 4.8 9.6
Point, (12) (−1) (3) (9) (15) (−10) (3) (10) (20)
Pa
(lb/100 ft2)
Gels, 9.6/18.2 61/92.9 14.4/ 10/22.5 3.8/11 2.4/5.3 2.9/4.3 5.3/13.9 2.9/11 1.4/5.7 2.9/3.8 8.1/20.6
Pa (20/38) (127/ 28.3 (21/47) (8/23) (5/11) (6/9) (11/29) (6/23) (3/12) (6/8) (17/43)
(lb/100 ft2) 194) (30/59)
API fluid 1.5 2.3 1.7 1.6 2.6 2.6 1.8 2.8 2.5 2.2 1.8 2.4
loss,
cm3/30 min
177° C. — — — 14 15 20 — 20 23 16 — 16
(350° F.)
HPHT
filtrate,
cm3/30 min
pH 8.5 9.0 6.9 9.0 9.8 9.1 9.2 9.0 8.9 8.9 9.8 8.6
Settling None

After 16 hours of static aging at about 260° C. (500° F.), all of the Formulas exhibited an HPHT filtrate of less than 25 cm3/min after 30 minutes at about 177° C. (350° F.). The result was believed to be attributable, at least in part, to the selection of polymer having desirable properties. Although not measured in this Example, one desirable property for the water soluble polymer is a 5% by weight Brookfield viscosity in freshwater of from about 50 cP to about 100 cP.
EXAMPLE 8
In the following test, the drilling fluid system had the following general formula, where the water soluble polymer was (D) 50:37.5:12.5 mole % acrylamide:AMPS:acrylate or (A) 10 mole % AMPS polymerized with acrylamide. The formulas and the results are given in the following Table:
Formulation
29 30 31 32
Experimental Water Soluble Polymer
D D A A
Freshwater, 196 196 196 196
ml(bbl) (0.56) (0.56) (0.56) (0.56)
MIL-GEL ™, 2.3 1.1 2.3 2.3
kg(lb) (4.0) (2.5) (4.0) (4.0)
MIL-TEMP ®, 1.1 1.1 0.9 0.9
kg(lb) (2.5) (2.5) (2.0) (2.0)
CHEM-TROL ® 2.3 2.3 2.3 2.3
X, kg(lb) (5.0) (5.0) (5.0) (5.0)
Caustic soda, 0.23 0.23 0.23 0.23
kg(lb) (0.5) (0.5) (0.5) (0.5)
KEM- 0.23 0.23 0.5 0.5
SEAL ® PLUS, (0.5) (0.5) (1.0) (1.0)
kg(lb)
Experimental 0.9 0.9 0.9 0.9
Water Soluble (2.0) (2.0) (2.0) (2.0)
Polymer, kg(lb)
POLYDRILL ™, 3.2 3.2 3.2 3.2
kg(lb) (7.0) (7.0) (7.0) (7.0)
MIL-CARB ®, 4.5 4.5 4.5 4.5
kg(lb) (10) (10) (10) (10)
MIL-BAR ®, 248.4 248.4 248.4 248.4
kg(lb) (547.7) (547.7) (547.7) (547.7)
Formulation
29 30 31 32
FLUID PROPERTIES Fann 35 at 49° C. (120° F.)
260° C. 260° C. 260° C. 260° C.
(500° F.) (500° F.) (500° F.) (500° F.)
Static Static Static Static
Age 16 Age 16 Age 16 Age 16
Initial Hours Initial Hours Initial Hours Initial Hours
600 rpm 117 89 104 81 235 100 205 103
300 rpm 62 58 56 50 132 55 115 58
200 rpm 45 46 39 39 94 41 81 44
100 rpm 25 34 22 26 54 24 46 29
 6 rpm 4 18 3 13 8 5 7 10
 3 rpm 3 16 2 11 6 4 5 8
Plastic Viscosity, 55 31 48 31 103 45 90 45
Cp
Yield Point, 3.4 12.9 3.8 9.1 13.9 4.8 12 6.2
Pa (7) (27) (8) (19) (29) (10) (25) (13)
(lb/100 ft2)
Gels, 2.4/3.8 12.4/26.8 1.4/2.9 7.7/16.3 3.4/4.8 3.8/13 3.8/5.7 7.7/27.3
Pa (5/8) (26/56) (3/6) (16/34) (7/10) (8/27) (8/12) (16/57)
(lb/100 ft2)
API fluid loss, 1.5 2.8 2.5 3.0 1.2 2.2 1.8 2.2
cm3/30 min
177° C. (350° F.) — 16 — 17 — 23 — 24
HPHT filtrate,
cm3/30 min
pH 9.8 8.9 9.8 9.0 9.9 8.9 9.4 8.9
Settling

After 16 hours of static aging at about 260° C. (500° F.), all of the Formulas exhibited an HPHT filtrate of less than 25 cm3/min after 30 minutes at about 177° C. (350° F.). The result was believed to be attributable, at least in part, to the selection of polymer having desirable properties.
EXAMPLE 9
In the following test, the drilling fluid system had the following general formula, where the water soluble polymer was (A) 10 mole % AMPS polymerized with acrylamide; (C) 40 mole % AMPS polymerized with acrylamide; or (F) 90 weight percent NaAMPS (AMPS, sodium salt)/10 weight percent N,N-dimethylacrylamide. The formulas and the results are given in the following Table:
Formulation
33 34 35 36 37
Experimental Water Soluble Polymer
A C F F A
Freshwater, 196 196 196 196 196
ml(bbl) (0.56) (0.56) (0.56) (0.56) (0.56)
MIL-GEL ™, 2.3 2.3 2.3 2.3 2.3
kg (lb) (4.0) (4.0) (4.0) (4.0) (4.0)
MIL-TEMP ®, 0.9 0.9 0.9 0.9 †0.9
kg (lb) (2.0) (2.0) (2.0) (2.0) (2.0)
(ALL-TEMP)
CHEM-TROL ® 2.3 2.3 2.3 2.3 2.3
X, kg (lb) (5.0) (5.0) (5.0) (5.0) (5.0)
Caustic soda, 0.23 0.23 0.23 0.23 0.23
kg (lb) (0.5) (0.5) (0.5) (0.5) (0.5)
KEM- 0.5 0.5 — — 0.5
SEAL ® PLUS, (1.0) (1.0) (1.0)
lb
Experimental 0.9 0.9 — — 0.9
Water Soluble (2.0) (2.0) (2.0)
Polymer, kg (lb)
KEM-SEAL ® — — 1.4 1.4 —
PLUS (3.0) (3.0)
Experimental,
kg (lb)
POLYDRILL ™, 3.2 3.2 3.2 3.2 3.2
kg (lb) (7.0) (7.0) (7.0) (7.0) (7.0)
MIL-CARB ®, 4.5 4.5 4.5 4.5 4.5(10)
kg (lb) (10) (10) (10) (10)
MIL-BAR ®, 248.4 248.4 248.4 248.4 248.4
kg (lb) (547.7) (547.7) (547.7) (547.7) (547.7)
Formulation
33 34 35 36 37
FLUID PROPERTIES Fann 35 at 49° C. (120° F.)
260° C. 260° C. 260° C. 260° C. 260° C.
(500° F.) (500° F.) (500° F.) (500° F.) (500° F.)
Static Static Static Static Static
Age 16 Age 16 Age 16 Age 16 Age 16
Initial Hours Initial Hours Initial Hours Initial Hours Initial Hours
600 rpm 166 91 153 96 230 218 197 235 254 118
300 rpm 93 51 85 61 131 176 111 191 144 72
200 rpm 67 37 61 48 94 161 81 176 103 56
100 rpm 38 24 35 34 54 138 46 151 59 37
 6 rpm 7 6 6 11 9 104 7 115 9 10
 3 rpm 5 4 4 9 6 103 5 110 6 8
Plastic 73 40 68 35 99 42 86 44 110 46
Viscosity, cP
Yield Point, 9.6 5.3 8.1 12.4 14.8 64.2 12 70.4 16.3 12.4
Pa (20) (11) (17) (26) (32) (134) (25) (147) (34) (26)
(lb/100 ft2)
Gels, 3.4/5 5.2/18.2 2.9/4.3 10/28.2 3.8/5.7 55/76 3.4/4.8 60/84 3.8/5.7 9.6/29
Pa (7/10) (11/38) (6/9) (21/59) (8/12) (115/159) (7/10) (125/176) (8/12) (20/62)
(lb/100 ft2)
API fluid loss, 1.8 2.0 1.5 2.5 1.4 2.6 1.4 3.2 1.0 2.1
cm3/30 min
149° C. (300° F.) — 44 — 49 — 54 — 52 — 26
HPHT filtrate, (13 min)
cm3/30 min
pH 9.5 8.8 9.5 8.8 9.2 9.0 9.4 9.1 9.5 8.9
*20% mole weight AMPS, **40% mole weight AMPS
*** & ****lower molecular weight version of KEM-SEAL PLUS
†substituted MIL-TEMP with ALL-TEMP to check compatibility

After 16 hours of static aging at about 260° C. (500° F.), all of the Formulas for which a measurement was taken exhibited an HPHT filtrate of greater than 25 cm3/min after 30 minutes or less at about 149° C. (300° F.). Formula 37, the 10 mole % AMPS polymerized with acrylamide (A) exhibited a HPHT filtrate of 26 cm3/min after 30 minutes or less at about 149° C. (300° F.). The result was believed to be attributable to variability among commercially available polymers and a lack of synergistic benefits of both experimental polymers and KEMSEAL® PLUS.
EXAMPLE 10
In the following test, the drilling fluid system had the following general formula, where the water soluble polymer was (A) 10 mole % AMPS polymerized with acrylamide. The formulas and the results are given in the following Table:
Form.
40 41 42 43 44 45
Experiimental Water Soluble Polymer
A A A A A A
Fresh- 196 196 196 196 196 196
water, (0.56) (0.56) (0.56) (0.56) (0.56) (0.56)
ml(bbl)
MIL- 2.3 2.3 2.3 2.3 2.3 2.3
GEL ™, (4.0) (4.0) (4.0) (4.0) (4.0) (4.0)
kg (lb)
MIL- 0.9 0.9 0.9 0.9 0.9 0.9
TEMP ®, kg (2.0) (2.0) (2.0) (2.0) (2.0) (2.0)
(lb)
CHEM- 2.3 2.3 2.3 2.3 2.3 2.3
TROL ® X, (5.0) (5.0) (5.0) (5.0) (5.0) (5.0)
kg (lb)
Caustic 0.23 0.23 0.23 0.23 0.23 0.23
soda, kg (lb) (0.5) (0.5) (0.5) (0.5) (0.5) (0.5)
KEM- 0.5 0.5 0.5 0.5 0.5 0.5
SEAL ®® (1.0) (1.0) (1.0) (1.0) (1.0) (1.0)
PLUS,
kg (lb)
Experiimental 0.9 0.9 0.9 0.9 0.9 0.9
Water (2.0) (2.0) (2.0) (2.0) (2.0) (2.0)
Soluble
Polymer,
kg (lb)
POLY- 3.2 3.2 3.2 3.2 3.2 3.2
DRILL ™, (7.0) (7.0) (7.0) (7.0) (7.0) (7.0)
kg (lb)
MIL- 4.5 4.5 4.5 4.5 4.5 4.5
CARB ®, (10) (10) (10) (10) (10) (10)
kg (lb)
MIL- 248.4 248.4 248.4 248.4 248.4 248.4
BAR ®, (547.7) (547.7) (547.7) (547.7) (547.7) (547.7)
kg (lb)
Add 10% — 15.8 15.8 15.8 15.8 15.8
NaCl, 1(bbl) (0.1) (0.1) (0.1) (0.1) (0.1)
MAX- — — 2.3 4.5 — —
TROL ®, (5.0) (10)
kg (lb)
SOLTEX ®, — — — — 10 —
kg (lb)
SULFA- — — — — — 10
TROL ®,
kg)lb)
Form.
40 41 42 43 44 45
FLUID PROPERTIES Fann 35 at 49° C. (120° F.)
260° C. 260° C. 260° C. 260° C. 260° C. 260° C.
(500° F.) (500° F.) (500° F.) (500° F.) (500° F.) (500° F.)
Static Static Static Static Static Static
Age 16 Age 16 Age 16 Age 16 Age 16 Age 16
Initial Hours Initial Hours Initial Hours Initial Hours Initial Hours Initial Hours
600 rpm 235 100 134 70 156 83 165 73 75
300 rpm 132 55 74 42 87 54 113 46 53
200 rpm 94 41 52 34 62 45 92 36 42
100 rpm 54 24 30 26 36 32 65 28 33
 6 rpm 8 5 4 13 4 15 22 18 21
 3 rpm 6 4 3 11 2 12 21 16 19
Plastic 103 45 60 28 69 29 52 27 22
Viscosity, cP
Yield Point, 13.4 4.8 6.7 6.7 8.6 12 29.2 0.1 14.8
Pa (29) (10) (14) (14) (18) (25) (61) (19) (31)
(lb/100 ft2)
Gels, 3.4/4.8 3.8/13 2.4/4.3 10.5/27.3 2.4/6.7 10/23 14.4/26.8 11/23 13.9/27.3
Pa (7/10) (8/27) (5/9) (22/57) (5/14) (21/48) (30/56) (23/48) (29/57)
(lb/100 ft2)
API fluid 1.2 2.2 1.2 3.0 0.9 2.8 7.8 2.4 3.0
loss,
cm3/30 min
177° C. (350° F.) — 23 — NC — >100 NC NC 48
HPHT
filtrate,
cm3/30 min
Ph 9.9 8.9 9.1 8.5 9.0 8.5 8.5 8.5 8.5
Settling

After 16 hours of static aging at about 260° C. (500° F.), Formula 40 exhibited an HPHT filtrate of less than 25 cm3/min after 30 minutes at about 177° C. (350° F.). The remaining Formulas that were tested exhibited an HPHT filtrate of greater than 25 cm3/min after 30 minutes or less at about 177° C. (350° F.). The result was believed to be attributable to deleterious effects of salt to the base fluid. Only Formula 45, which included 10 lb/bbl SULFA-TROL®, exhibited restoration of HPHT filtration control.
EXAMPLE 12
In the following test, the drilling fluid system had the following general formula, where the water soluble polymer was (A) 10 mole % AMPS polymerized with acrylamide. The formulas and the results are given in the following Table:
Form.
50 51
46 47 48 49 (repeat #40)] [(re-mix) # 50]
Experiimental Water Soluble Polymer
A A A A A A
Fresh- 196 196 196 196 196 196
water, ml(bbl) (0.56) (0.56) (0.56) (0.56) (0.56) (0.56)
MIL- 2.3 2.3 2.3 2.3 2.3 2.3
GEL ™, (4.0) (4.0) (4.0) (4.0) (4.0) (4.0)
kg (lb)
MIL- 0.9 0.9 0.9 0.9 0.9 0.9
TEMP ®, (2.0) (2.0) (2.0) (2.0) (2.0) (2.0)
kg (lb)
CHEM- 2.3 2.3 2.3 2.3 2.3 2.3
TROL ® X, (5.0) (5.0) (5.0 (5.0) (5.0) (5.0)
kg (lb)
Caustic 0.23 0.23 0.23 0.23 0.23 0.23
soda, kg (lb) (0.5) (0.5) (0.5) (0.5) (0.5) (0.5)
KEM- 0.5 0.5 0.5 0.5 0.5 0.5
SEAL ® (1.0) (1.0) (1.0) (1.0) (1.0) (1.0)
PLUS, kg (lb)
Experiimental 0.9 0.9 0.9 0.9 0.9 0.9
Water (2.0) (2.0) (2.0) (2.0) (2.0) (2.0)
Soluble
Polymer,
kg (lb)
POLY- 3.2 3.2 3.2 3.2 3.2 3.2
DRILL ™, (7.0) (7.0) (7.0) (7.0) (7.0) (7.0)
kg (lb)
MIL- 4.5 4.5 4.5 4.5 4.5 4.5
CARB ®, (10) (10) (10) (10) (10) (10)
kg (lb)
MIL- 248.4 248.4 248.4 248.4 248.4 248.4
BAR ®, kg (lb) (547.7) (547.7) (547.7) (547.7) (547.7) (547.7)
Add 10% 15.8 15.8 15.8 15.8 — —
NaCl, 1(bbl) (0.1) (0.1) (0.1) (0.1)
SULFA- — 2.3 4.5 — — —
TROL ®, (5.0) (10)
kg (lb)
PROTECTO- 4.5 2.3 — — — —
MAGIC ™, (10) (5.0)
kg (lb)
CHEK- — — 4.5 — — —
LOSS ® (10)
PLUS, kg)lb)
Bore-Drill, — — — 4.5 — —
kg (lb) (10)
Form.
50 51
FLUID PROPERTIES Fann 35 at 49° C. (120° F.)
260° C. 260° C. 260° C. 260° C. 260° C. 260° C.
(500° F.) (500° F.) (500° F.) (500° F.) (500° F.) (500° F.)
Static Static Static Static Static Static
Age 16 Age 16 Age 16 Age 16 Age 16 Age 16
Initial Hours Initial Hours Initial Hours Initial Hours Initial Hours Initial Hours
600 rpm 126 81 111 Cannot 260 100 247 73
300 rpm 93 57 77 Stir 140 52 137 39
200 rpm 81 48 70 Down 105 36 98 26
100 rpm 66 37 58 58 20 56 14
 6 rpm 49 25 40 8 3 8 2
 3 rpm 47 23 39 6 2 6 1
Plastic 33 24 34 120 48 110 34
Viscosity, cP
Yield Point, 28.7 11 20.6 9.6 1.9 12.9 2.4
Pa (60) (23) (43) (20) (4) (27) (5)
(lb/100 ft2)
Gels, 24.9/36.4 15.8/33.5 27.3/52.7 3.8/4.8 1.4/11 3.4/5.2 .96/6.7
Pa (51/76) (33/70) (57/110) (8/10) (3/23) (7/11) (2/14)
(lb/100 ft2)
API fluid 2.8 2.8 2.2 1.0 1.7 1.0 2.0
loss, cm3/30 min
177° C. (350° F.) 62 80 80 — 44 — 46
HPHT
filtrate,
cm3/30 min
pH 8.3 8.4 8.3 9.5 8.9 9.1 8.8

After 16 hours of static aging at about 260° C. (500° F.), all of the Formulas tested exhibited an HPHT filtrate of greater than 25 cm3/min after 30 minutes at about 177° C. (350° F.). The result was believed to be attributable to the deleterious effects of salt and variability among commercially available polymers. Testing with other commercially available additives did not restore HPHT filtration control.
EXAMPLE 13
In the following test, the drilling fluid system had the following general formula, where the water soluble polymer was (A) 10 mole % AMPS polymerized with acrylamide. The formulas and the results are given in the following Table:
Formulation
52 53 54 55 56 57
Experimental Water Soluble Polymer
A A A A A A
Fresh- 196 196 196 196 196 196
water, ml(bbl) (0.56) (0.56) (0.56) (0.56) (0.56) (0.56)
MIL- 2.3 2.3 2.3 2.3 2.3 2.3
GEL ™, (4.0) (4.0) (4.0) (4.0) (4.0) (4.0)
kg(lb)
MIL- 0.9 0.9 0.9 0.9 0.9 0.9
TEMP ®, (2.0) (2.0) (2.0) (2.0) (2.0) (2.0)
kg(lb)
CHEM- 2.3 2.3 2.3 2.3 2.3 2.3
TROL ® X, (5.0) (5.0) (5.0) (5.0) (5.0) (5.0)
kg(lb)
Caustic 0.23 0.23 0.23 0.23 0.23 0.23
soda, kg(lb) (0.5) (0.5) (0.5) (0.5) (0.5) (0.5)
KEM- 0.5 0.5 0.5 0.5 0.5 0.5
SEAL ® (1.0) (1.0) (1.0) (1.0) (1.0) (1.0)
PLUS, kg(lb)
Experimental 0.9 0.9 0.9 0.9 0.9 0.9
Water (2.0) (2.0) (2.0) (2.0) (2.0) (2.0)
Soluble
Polymer,
kg(lb)
POLY- 3.2 3.2 3.2 3.2 3.2 3.2
DRILL ™, (7.0) (7.0) (7.0) (7.0) (7.0) (7.0)
kg(lb)
MIL- 4.5 4.5 4.5 4.5 4.5 4.5
CARB ®, (10) (10) (10) (10) (10) (10)
kg(lb)
MIL- 248.4 248.4 248.4 248.4 248.4 248.4
BAR ®, kg(lb) (547.7) (547.7) (547.7) (547.7) (547.7) 547.7
Add 10% 15.8 15.8 — — — —
NaCl, l(bbl) (0.1) (0.1)
SULFA- — 5 — — — —
TROL ®,
kg(lb)
BORE- 2.3 2.3 — — — —
DRILL ™, (5) (5)
kg(lb)
Form.
52 53 54 55 56 57
FLUID PROPERTIES Fann 35 at 49° C.(120° F.)
260° C. 260° C. 260° C. 260° C. 260° C. 260° C.
(500° F.) (500° F.) (500° F.) (500° F.) (500° F.) (500° F.)
Static Static Static Static Static Static
Age 16 Age 16 Age 16 Age 16 Age 16 Age 16
Initial Hours Initial Hours Initial Hours Initial Hours Initial Hours Initial Hours
600 rpm 197 227 274 93 192 125 189 110 174 103
300 rpm 140 160 153 52 103 65 104 58 95 57
200 rpm 116 136 110 38 72 47 75 42 67 41
100 rpm 87 100 62 22 41 28 42 24 38 24
6 rpm 40 43 8 4 7 9 7 5 6 5
3 rpm 35 40 6 3 5 7 5 3 4 3
Plastic 37 67 121 41 89 60 85 52 79 46
Viscosity, Cp
Yield Point, 49.3 44.5 15.3 5.3 6.7 2.4 9.1 2.9 7.7 5.3
Pa (103) (93) (32) (11) (14) (5) (19) (6) (16) (11)
(lb/100 ft2)
Gels, 23/43.6 24.449.8 3.4/5.7 3.4/13.4 2.9/5.3 8.1/25.9 2.9/4.8 3.8/15.8 2.9/ 4.9/20.1
Pa (48/91) (51/104) (7/12) (7/28) (6/11) (17/54) (6/10) (8/33) 4.3 (10/42)
(lb/100 ft2) (6/9)
API fluid 3.8 5.4 1.4 2.0 1.2 2.4 1.0 2.2 1.2 2.2
loss, cm3/
30 min
177° C. — — — 50 — 38 — 28 — 40
(350° F.)
HPHT
filtrate,
cm3/30 min
pH 8.2 8.5 9.6 8.7 9.7 8.7 9.7 8.7 9.8 8.8
Settling

After 16 hours of static aging at about 260° C. (500° F.), all of the Formulas tested exhibited an HPHT filtrate of greater than 25 cm3/min after 30 minutes at about 177° C. (350° F.). The result was believed to be attributable, at least in part, to variability among commercially available polymers.
EXAMPLE 14
In the following test, the drilling fluid system had the following general formula, where the water soluble polymer was (A) 10 mole % AMPS polymerized with acrylamide. The formulas and the results are given in the following Table:
Formulation
58 59 60
Experimental Water Soluble Polymer
A A A
Freshwater, 196 196 196
ml(bbl) (0.56) (0.56) (0.56)
MIL-GEL ™, 2.3 2.3 2.3
kg(lb) (4.0) (4.0) (4.0)
MIL-TEMP ®, 0.9 0.9 0.9
kg(lb) (2.0) (2.0) (2.0)
CHEM-TROL ® 2.3 2.3 2.3
X, kg(lb) (5.0) (5.0) (5.0)
Caustic soda, 0.23 0.23 0.23
kg(lb) (0.5) (0.5) (0.5)
KEM- 0.5 0.5 0.5
SEAL ®PLUS, (1.0) (1.0) (1.0)
kg(lb)
Experimental 2 2 2
Water Soluble
Polymer, kg(lb)
POLYDRILL ™, 3.2 3.2 3.2
kg(lb) (7.0) (7.0) (7.0)
MIL-CARB ®, 4.5 4.5 4.5
kg(lb) (10) (10) (10)
MIL-BAR ®, 248.4 248.4 248.4
kg(lb) (547.7) (547.7) (547.7)
10% NaCl, l(bbl) — 15.8 15.8
(0.1) (0.1)
SULFA- — 4.5
TROL ®, kg(lb, (10)
POLYDRILL ™, — — 4.5
kg(lb) (10)
Formulation
58 59 60
FLUID PROPERTIES Fann 35 at 49° C.(120° F.)
260° C. 260° C. 260° C. 260° C.
(500° F.) (500° F.) (500° F.) (500° F.)
Static Static Static Static
Age 16 Age 72 Age 16 Age 16
Initial Hours Hours Hours Hours
600 rpm 216 90 77 104 113
300 rpm 120 51 45 76 84
200 rpm 86 39 32 65 70
100 rpm 48 24 19 52 58
6 rpm 8 5 4 30 37
3 rpm 5 4 3 29 35
Plastic 96 39 32 28 29
Viscosity, Cp
Yield Point, 11.5 5.7 6.2 23 26.3
Pa(lb/100 ft2) (24) (12) (13) (48) (55)
Gels, 3.8/ 4.8/20.1 2.4/13.4 19.6/38.3 20.6/35.4
Pa 10.5 (10/42) (5/28) (41/80) (43/74)
(lb/100 ft2) (8/
22)
API fluid loss, 1.6 2.4 2.4 2.4 2.0
cm3/30 min
177° C.(350° F.) — 34 20 24 NC
HPHT filtrate,
cm3/30 min
pH 9.6 8.7 8.5 8.3 8.3

After 16 hours of static aging at about 260° C. (500° F.), Formulas 58 (no added NaCl) and 59 (10 lb/bbl SULFA-TROL® and added NaCl) exhibited an HPHT filtrate of less than 25 cm3/min after 30 minutes at about 177° C. (350° F.). Formula 60, which contained added NaCl, but not SULFA-TROL®, exhibited an HPHT filtrate of greater than 25 cm3/min after 30 minutes at about 177° C. (350° F.).
EXAMPLE 15
In the following test, the drilling fluid system had the following general formula, where the water soluble polymer was (A) 10 mole % AMPS polymerized with acrylamide. The formulas and the results are given in the following Table:
Formulation
61 62 63 64 65 66
Experimental Water Soluble Polymer
**16-hr
aged
A sample A A A A
Fresh- 196 196 196 196 196
water, (0.56) (0.56) (0.56) (0.56) (0.56)
ml(bbl)
MIL-GEL ™, 2.3 2.3 2.3 2.3 2.3
kg(lb) (4.0) (4.0) (4.0) (4.0) (4.0)
MIL-TEMP ®, 0.9 0.9 0.9 0.9 0.9
kg(lb) (2.0) (2.0) (2.0) (2.0) (2..0)
CHEM-TROL ® X, 2.3 2.3 2.3 2.3 2.3
kg(lb) (5.0) (5.0) (5.0) (5.0) (5.0)
Caustic soda, 0.23 0.23 0.23 0.23 0.23
kg(lb) (0.5) (0.5) (0.5) (0.5) (0.5)
KEM-SEAL ®® 0.5 0.5 0.5 0.5 0.5
PLUS, kg(lb) (1.0) (1.0) (1.0) (1.0) (1.0)
Experimental 0.9 0.9 0.9 0.9 0.9
Water Soluble (2) (2) (2) (2) (2)
Polymer, kg(lb)
POLYDRILL ™, 3.2 3.2 3.2 3.2 3.2
kg(lb) (7.0) (7.0) (7.0) (7.0) (7.0)
MIL-CARB ®, 4.5 4.5 4.5 4.5 4.5
kg(lb) (10) (10) (10) (10) (10)
MIL-BAR, 248.4 248.4 248.4 248.4 248.4
kg(lb) (547.7) (547.7) (547.7) (547.7) (547.7)
10% NaCl ®, — 15.8 15.8 15.8 15.8 15.8
l(bbl) (0.1) (0.1) (0.1) (0.1) (0.1)
SULFA-TROL ®, — 4.5 4.5 2.3 2.3
kg(lb) (10) (10) (5.0) (5.0)
POLYDRILL ™, — — 4.5 —
kg(lb) (10)
PROTECTO- — — — — 2.3
MAGIC, (5.0)
kg(lb)
Caustic soda, kg(lb — 0.23 — — — —
(0.5)
Form.
61 62 63 64 65 66
FLUID PROPERTIES Fann 35 at 149° C. (120° F.)
260° C. 260° C. 260° C. 260° C. 260° C.
(500° F.) (500° F.) (500° F.) 260° C. 260° C. (500° F.) (500° F.)
Static Static Static (500° F.) (500° F.) Static Static
Age 16 Age 72 Age 16 Static Age Static Age Age 16 Age 16
Initial Hours Hours Hours 16 Hours 16 Hours Hours Hours
600 rpm 216 90 77 133 104 113 116 143
300 rpm 120 51 45 103 76 84 85 110
200 rpm 86 39 32 92 65 70 75 98
100 rpm 48 24 19 77 52 58 60 84
6 rpm 8 5 4 55 30 37 40 60
3 rpm 5 4 3 52 29 35 37 57
Plastic Viscosity, 96 39 32 30 28 29 31 33
cP
Yield Point, 11.5 5.7 6.2 35 23 26.3 25.9 36.9
Pa (24) (12) (13) (73) (48) (55) (54) (77)
(lb/100 ft2)
Gels, Pa 3.8/10.5 4.8/20.1 2.4/13.4 29.6/49.3 19.6/38.3 20.6/35.4 24/49.8 32.6/55
(lb/100 ft2) (8/22) (10/42) (5/28) (62/103) (41/80) (43/74) (50/104) (68/115)
API fluid loss, 1.6 2.4 2.4 2.0 2.4 2.0 2.8 3.0
cm3/30 min
177° C.(350° F.) — 34 20 22 24 NC >100 86
HPHT
filtrate,
cm3/30 min
Ph 9.6 8.7 8.5 8.5 8.3 8.3 8.4 8.3
**16-hr aged sample was sample 61, which was already aged at 500° F. for 16 hours, and then was contaminated with 10% by vol. 10% NaCl brine, followed with 10 lb/bbl SULFA-TROL ® and 0.23(0.5) lb/bbl caustic soda

After 16 hours of static aging at about 260° C. (500° F.), Formula 63 and reaged Formula 62, which contained both NaCl and SULFA-TROL®, exhibited an HPHT filtrate of less than 25 cm3/min after 30 minutes at about 177° C. (350° F.). The remainder of the formulas exhibited an HPHT filtrate of greater than 25 cm3/min after 30 minutes or less at about 177° C. (350° F.).
EXAMPLE 16
In the following test, the drilling fluid system had the following general formula, where the water soluble polymer was (A) 10 mole % AMPS polymerized with acrylamide. The formulas and the results are given in the following Table:
Form.
67 68 69 70 71 72
Experimental Water Soluble Polymer
A A A A A A
Fresh- 196 196 196 196 196 196
water, (0.56) (0.56) (0.56) (0.56) (0.56) (0.56)
ml(bbl)
MIL-GEL ™, 2.3 2.3 2.3 2.3 2.3 2.3
kg(lb) (4.0) (4.0) (4.0) (4.0) (4.0) (4.0)
MIL- 0.9 0.9 0.9 0.9 0.9 0.9
TEMP ®, (2.0) (2.0) (2.0) (2.0) (2.0) (2.0)
kg(lb)
CHEM- 2.3 2.3 2.3 2.3 2.3 2.3
TROL ® X, (5.0) (5.0) (5.0) (5.0) (5.0) (5.0)
kg(lb)
Caustic 0.23 0.23 0.23 0.23 0.23 0.23
soda, kg(lb) (0.5) (0.5) (0.5) (0.5) (0.5) (0.5)
KEM- 0.5 0.5 0.5 0.5 0.5 0.5
SEAL ® (1.0) (1.0) (1.0) (1.0) (1.0) (1.0)
PLUS, kg(lb)
Experimental 0.9 0.9 0.9 0.9 0.9 2.3
Water (2) (2) (2) (2) (2.0) (4.0)
Soluble
Polymer,
kg(lb)
POLY- 3.2 3.2 3.2 3.2 3.2 3.2
DRILL ™, (7.0) (7.0) (7.0) (7.0) (7.0) (7.0)
(kg/lb)
MIL- 4.5 4.5 4.5 4.5 4.5 4.5
CARB ®, kg(lb) (10) (10) (10) (10) (10) (10)
MIL-BAR ®, 248.4 248.4 248.4 248.4 248.4 248.4
kg(lb) (547.7) (547.7) (547.7) (547.7) (547.7) (547.7)
10% — 15.8 15.8 15.8 — —
NaCl, l(bbl) (0.1) (0.1) (0.1)
SULFA- — 4.5 — — — —
TROL ®, (10)
kg(lb)
MAX- — — 4.5 — — —
TROL ®, (10)
kg(lb)
SOLTEX ®, — — 4.5 — —
kg(lb) (10)
Form.
67 68 69 70 71 72
FLUID PROPERTIES Fann 35 at 49° C.(120° F.)
260° C. 260° C. 260° C. 260° C. 260° C. 260° C.
(500° F.) (500° F.) (500° F.) (500° F.) (500° F.) (500° F.)
Static Static Static Static Static Static
Age 16 Age 16 Age 16 Age 16 Age 16 Age 16
Initial Hours Initial Hours Initial Hours Initial Hours Initial Hours Initial Hours
600 rpm 182 102 220 101 >300 77 264 70
300 rpm 99 72 159 75 >300 36 145 40
200 rpm 70 60 134 64 224 22 103 31
100 rpm 39 48 103 52 131 12 58 19
6 rpm 6 30 48 33 21 2 9 7
3 rpm 4 27 42 31 17 1 6 6
Plastic 83 30 61 26 NM 41 119 30
Viscosity, Cp
Yield Point, 7.7 20.1 46.9 23.5 NM 0 12.4 4.8
Pa (16) (42) (98) (49) (0) (26) (10)
(lb/100 ft2)
Gels, 2.9/ 17.7/29.7 27.3/43.6 17.7/26.3 9.6/16.3 1.9/4.3 3.8/8.6 5.3/11.5
Pa 3.8 (37/62) (57/91) (37/55) (20/34) (4/9) (8/18) (11/24)
(lb/100 ft2) (6/8)
API fluid 1.5 2.3 4.4 2.7 2.0 2.0 1.8 2.6
loss, cm3/30 min
177° C.(350° F.) — 21 60 >100 — 16 — 18
HHPT
filtrate,
cm3/30 min
pH 9.8 8.5 9.0 8.6 7.9 8.6 8.1 8.5
After 16 hours of static aging at about 260° C. (500° F.), the control (no added NaCl, Formulas 71 and 72) and Formula 68 (containing 10 lb.bbl SULFA-TROL®) exhibited an HPHT filtrate of less than 25 cm3/min after 30 minutes at about 177° C. (350° F.). The remainder of the formulas exhibited an HPHT filtrate of greater than 25 cm3/min after 30 minutes or less at about 177° C. (350® F.). This was true even though Formula 70 contained SOLTEX®, a sulfonated asphalt product. The result was believed to be attributable to the fact that SULFA-TROL® has a % lignite content. Lignite has limited solubility in saline water, which may account for improved HPHT filtration control compared with SOLTEX®. It is believed that the insoluble portion of the colloidal lignite will impart particle plugging onto the filter cake, thereby slowing down filtration. SOLTEX® apparently is too soluble to impart particle plugging.
In order to determine the differences between the two sulfonated asphalts, a measurement was made of “High pH Soluble but Low pH Insoluble” Materials for SOLTEX® and SULFA-TROL® Samples, as compared to LIGCO® (pure lignite)
Samples LIGCO ® SOLTEX ® SULFA-TROL ®
% soluble at pH = 11 but 77% 0.5% (test 1) 28% (test 1)
insoluble at pH = 2.5 0.8% (test 2) 25% (test 2)
% “Lignite” content* 100%   1% 34%
*Note: Calculated based on that lignite is 77% soluble at pH = 11.
EXAMPLE 17
In the following test, the drilling fluid system had the following general formula, where the water soluble polymer was (A) 10 mole % AMPS polymerized with acrylamide. Each of the formulations contained 10 lb/bbl SULFA-TROL®, with varying levels of NaCl. The formulas and the results are given in the following Table:
Formulation
73 74 75 76
Experimental Water Soluble Polymer
A A A A
Freshwater, ml(bbl) 196 196 196 196
(0.56) (0.56) (0.56) (0.56)
MIL-GEL ™, kg(lb) 2.3 2.3 2.3 2.3
(4.0) (4.0) (4.0) (4.0)
NaCI, kg(lb) 1.8 1.8 3.6 3.6
(3.9) (3.9) (8.0) (8.0)
MIL-TEMP ®, kg(lb 0.9 0.9 0.9 0.9
(2.0) (2.0) (2.0) (2.0)
CHEM-TROL ® X, kg(lb) 2.3 2.3 2.3 2.3
(5.0) (5.0) (5.0) (5.0)
Caustic soda, kg(lb) 0.23 0.23 0.23 0.23
(0.5) (0.5) (0.5) (0.5)
KEM-SEAL ® PLUS, 0.5 0.5 0.5 0.5
kg(lb) (1.0) (1.0) (1.0) (1.0)
Experimental Water 0.9 — 0.9 —
Soluble Polymer, kg(lb) (2.0) (2.0)
POLYDRILL ™, kg(lb) 3.2 3.2 3.2 3.2
(7.0) (7.0) (7.0) (7.0)
MIL-CARB ®, kg(lb) 4.5 4.5 4.5 4.5
(10) (10) (10) (10)
MIL-BAR ®, kg(lb) 248.4 248.4 248.4 248.4
(547.7) (547.7) (547.7) (547.7)
SULFA-TROL ®, kg(lb) 4.5 4.5 4.5 4.5
(10) (10) (10) (10)
Formulation
73 74 75 76
FLUID PROPERTIES Fann 35 at 49° C. (120° F.)
260° C. 260° C. 260° C.
(500° F.) (500° F.) (500° F.) 260° C.
Static Static Static (500° F.)
Age 16 Age 16 Age 16 Static Age
Initial Hours Initial Hours Initial Hours Initial 16 Hours
600 rpm 190 159 109 181 172 127 107 105
300 rpm 104 113 62 142 95 87 60 80
200 rpm 75 95 44 128 67 71 43 71
100 rpm 42 74 26 109 38 55 26 59
 6 rpm 6 45 4 85 6 34 5 47
 3 rpm 4 42 3 82 3 31 4 44
Plastic Viscosity, cP 86 46 47 39 77 40 47 25
Yield Point, 8.6 32 7.2 49.3 8.6 22.5 6.2 26.3
Pa (18) (67) (15) (103) (18) (47) (13) (55)
(lb/100 ft2)
Gels, Pa 3.4/8.6 25.4/39.3 3.4/6.2 3.4/47.4 3.4/10 18.7/29.6 3.8/8.6 20.6/33.5
(lb/100 ft2) (7/18) (53/82) (7/13) (7/99) (7/21) (39/62) (8/18) (43/70)
API fluid loss, cm3/30 0.9 2.0 0.6 2.5 1.0 2.0 1.5 2.7
min
177° C. (350° F.) HPHT — 19 — NC — NC — NC
filtrate,
cm3/30 min
Ph 9.1 8.6 9.3 8.9 8.9 8.2 9.0 8.6

After 16 hours of static aging at about 260° C. (500° F.), the only formula tested that exhibited an HPHT filtrate of less than 25 cm3/min after 30 minutes at about 177° C. (350° F.) was Formula 73, which contained 2 lb/bbl of the experimental water soluble polymer, 3.9 lb/bbl NaCl (or about 9000 ppm NaCl) and 10 lb/bbl SULFA-TROL®. Examples 75 and 76 contained 8.0 lb/bbl NaCl, or from about 18,000 to about 20,000 ppm NaCl, and Example 76 did not include the experimental water soluble polymer.
Persons of ordinary skill in the art will recognize that many modifications may be made to the foregoing without departing from the spirit and scope thereof. The embodiment described herein is meant to be illustrative only and should not be taken as limiting the invention, which is defined in the following claims.

Claims (10)

1. A drilling fluid system comprising:
an aqueous base consisting essentially of freshwater;
bridging agent comprising from about 0.7 to about 29 kg/m3 (0.25 lb/bbl to about 10.0 lb/bbl) water soluble polymer having a 5% by weight Brookfield viscosity in freshwater of from about 50 cP to about 100 cP, said water soluble polymer comprising from about 10 to about 20 mole % monomer of acrylamide, from about 50 to about 60 mole % monomer of 2-acrylamido-2-methylpropane sulfonic acid or alkali metal salts thereof, and from about 25 to about 35 mole % N-vinyl pyrrolidone monomer; and,
from about 21.42 to 57.15 kg/m3 (7.5 to 20 lb/bbl) plugging agent comprising sulfonated asphalt and lignite;
wherein, after 16 hours of static aging of the drilling fluid system at about 260° C. (500° F.), the drilling fluid system exhibits a HPHT filtrate of 25 cm3/min or less after 30 minutes at about 149° C. (300° F.).
2. The drilling fluid system of claim 1 exhibiting a HPHT filtrate of 25 cm3/min or less after 30 minutes at about 177° C. (350° F.).
3. The drilling fluid system of claim 1 exhibiting said HPHT filtrate at a content of 10,000 ppm or less monovalent salt and the plugging agent comprises from about 20 wt. % to about 30 wt. % lignite.
4. The drilling fluid system of claim 1 exhibiting said HPHT filtrate at a content of 9,000 ppm or less monovalent salt, wherein said amount of water soluble polymer is from about 2.8 to about 11.5 kg/m3(1 to about 4 lb/bbl).
5. The drilling fluid system of claim 1 wherein said water soluble polymer comprises:
about 55 mole % 2-acrylamido-2-methylpropane sulfonic acid; and,
about 30 mole % N-vinyl pyrrolidone; and
about 15 mole % acrylamide.
6. A drilling fluid system comprising:
an aqueous base consisting essentially of freshwater;
bridging agent comprising from about 0.7 to about 29 kg/m3(0.25 lb/bbl to about 10.0 lb/bbl) water soluble polymer having a 5% by weight Brookfield viscosity in freshwater of from about 50 to about 100 cP comprising from about 90 to about 80 mole % monomers of acrylamide and from about 10 to about 20 mole % 2-acrylamido-2-methylpropane sulfonic acid or alkali metal salts thereof; and,
plugging agent comprising a quantity of from about 21 to 58 kg/m3(7.5 to 20 lb/bbl) sulfonated asphalt comprising lignite;
wherein, after 16 hours of static aging of the drilling fluid system at about 260° C. (500° F.), the drilling fluid system exhibits a HPHT filtrate of 25 cm3/min or less after 30 minutes at about 149° C. (300° F.).
7. The drilling fluid system of claim 6 exhibiting a HPHT filtrate of 25 cm 3/min or less after 30 minutes at about 177° C. (350° F.).
8. The drilling fluid system of claim 6 exhibiting said HPHT filtrate at a content of 10,000 ppm or less monovalent salt and the plugging agent comprises from about 20 wt. % to about 30 wt. % lignite.
9. The drilling fluid system of claim 6 exhibiting said HPHT filtrate at a content of 9,000 ppm or less monovalent salt, wherein said amount of water soluble polymer is from about 2.8 to about 11.5 kg/m3 (1 to about 4 lb/bbl).
10. The drilling fluid system of claim 6 wherein said water soluble polymer comprising
about 55 mole % 2-acrylamido-2-methylpropane sulfonic acid; and,
about 15 mole % acrylamide.
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